WO2020067148A1 - Waste treatment device - Google Patents

Waste treatment device Download PDF

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Publication number
WO2020067148A1
WO2020067148A1 PCT/JP2019/037579 JP2019037579W WO2020067148A1 WO 2020067148 A1 WO2020067148 A1 WO 2020067148A1 JP 2019037579 W JP2019037579 W JP 2019037579W WO 2020067148 A1 WO2020067148 A1 WO 2020067148A1
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WO
WIPO (PCT)
Prior art keywords
unit
processing
waste disposal
disposal apparatus
control unit
Prior art date
Application number
PCT/JP2019/037579
Other languages
French (fr)
Japanese (ja)
Inventor
道太郎 牧
福本 克久
弘明 渡邊
Original Assignee
株式会社Lixil
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from JP2018185503A external-priority patent/JP2020055132A/en
Priority claimed from JP2018183080A external-priority patent/JP2020049446A/en
Priority claimed from JP2018183078A external-priority patent/JP7177648B6/en
Priority claimed from JP2018185510A external-priority patent/JP2020054937A/en
Priority claimed from JP2018183079A external-priority patent/JP2020049445A/en
Application filed by 株式会社Lixil filed Critical 株式会社Lixil
Publication of WO2020067148A1 publication Critical patent/WO2020067148A1/en

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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/01Deodorant compositions
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/14Disinfection, sterilisation or deodorisation of air using sprayed or atomised substances including air-liquid contact processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/38Removing components of undefined structure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B5/00Operations not covered by a single other subclass or by a single other group in this subclass

Definitions

  • the present disclosure relates to a waste disposal apparatus.
  • Japanese Utility Model Registration No. 3139358 discloses a separation tank to which water, a polymer separating agent and a sterilizing / sterilizing agent are supplied, and a stirrer for stirring the processed material in the separation tank.
  • a used paper diaper separating and collecting apparatus for separating and collecting diapers used paper diapers put in a collecting body are put into a separation tank, and crushing means for crushing the collected body and the used paper diaper are provided. Is disclosed.
  • JP-A-2018-24964 discloses a method for recovering pulp fibers from used absorbent articles. This method dissolves the hot melt or the adhesive tape by adding an aqueous solution containing a terpene to a disposable diaper in which the top sheet and the back sheet are fixed with a hot melt or an adhesive tape, and forms the top sheet and the back sheet of the disposable diaper. It is possible to take out the pulp or the high-molecular polymer separated and separated between the top sheet and the back sheet.
  • Japanese Patent Application Laid-Open No. 2000-84533 discloses a method of recycling used materials for used disposable diapers.
  • the recycling equipment that performs this method can crush the paper diaper and then decompose the polymer in a polymer decomposition tank to recover vinyl and pulp.
  • JP-A-2000-84533 discloses a disposal facility for disposing of used paper diapers as an object to be treated.
  • This disposal facility can separate the disposable diaper from the water absorbed by the disposable diaper polymer.
  • the high-molecular-weight water-absorbing polymer contained in the disposable diaper is reacted with a polymer-decomposing agent as a treating agent, and water is extracted from the high-molecular-weight water-absorbing polymer.
  • water is separated from the polymer by performing the treatment in a crusher, a polymer decomposition tank, a stirring tank, or the like.
  • the first waste disposal apparatus has been made in view of the above-mentioned conventional circumstances, and an object of the present invention is to provide a waste disposal apparatus capable of suppressing the rise of odor in a room.
  • the second waste disposal apparatus has been made in view of the above-mentioned conventional circumstances, and has as an object to provide a waste disposal apparatus that can operate well.
  • the third waste disposal apparatus has been made in view of the above-mentioned conventional circumstances, and has as an object to solve the problem of providing a more compact waste disposal apparatus.
  • the fourth waste disposal apparatus has been made in view of the above-mentioned conventional situation, and an object of the present invention is to provide a waste disposal apparatus capable of suppressing the occurrence of problems due to excess or deficiency of the treatment agent. I have.
  • the fifth waste disposal apparatus has been made in view of the above-described conventional situation, and has as an object to solve the problem of providing a waste disposal apparatus capable of more accurately grasping the status of the processing unit.
  • the first waste treatment apparatus is connected to a charging unit that inputs a waste having a polymer capable of absorbing and retaining moisture, a crushing unit that crushes the waste to make the crushed material, and a connection port of the input unit, A deodorizing device for deodorizing odors generated from at least one of filth and the crushed material.
  • the second filth treatment apparatus includes: an input section for inputting filth having a polymer capable of absorbing and retaining moisture; and a processing section for separating and processing the filth; a processing mode for separating and processing the filth; And a cleaning mode for cleaning the unit.
  • the cleaning unit includes a discharge unit that discharges at least one of water and hot water in the cleaning mode.
  • the third waste treatment apparatus separates waste having a polymer capable of absorbing and retaining moisture, includes a plurality of treatment units connected in series, and the treatment unit on the downstream side can be treated in one treatment.
  • the amount is equal to or more than the processing amount that can be processed by the processing unit on the upstream side in one process.
  • a fourth waste treatment apparatus includes a charging section into which a processing object having a water-absorbing polymer is charged, and a processing section configured to process the processing object using a processing agent for suppressing water absorption performance of the polymer. And a control unit that has a determination unit that determines a state of the processing object input from the input unit, and determines an input amount of the processing agent based on the state of the processing object determined by the determination unit. And
  • the fifth filth disposal apparatus is a processing unit that performs processing on a processing target having a water-absorbing polymer using a processing agent for suppressing the water absorbing performance of the polymer, and information on an operation state of the processing unit.
  • FIG. 1 is a schematic diagram of a waste disposal apparatus of Embodiment 1 of the first waste disposal apparatus
  • FIG. 2 is a schematic diagram of a waste disposal apparatus of Embodiment 2 of the first waste disposal apparatus
  • FIG. 3 is a schematic diagram of a waste disposal apparatus of Embodiment 3 of the first waste disposal apparatus
  • FIG. 4 is a schematic diagram of a waste disposal apparatus of Embodiment 4 of the second waste disposal apparatus
  • FIG. 5 is a schematic diagram of a waste disposal apparatus of Embodiment 3 of the third waste disposal apparatus
  • FIG. 6 is a schematic diagram of a waste disposal apparatus of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus
  • FIG. 7 is a block diagram schematically illustrating a configuration of a control system of the waste disposal apparatus according to Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus.
  • FIG. 8 is a graph showing an example of a change in current consumption of a motor when processing a processing object in a processing unit according to the sixth embodiment of the fourth waste processing apparatus and the fifth waste processing apparatus;
  • FIG. 9 is a graph illustrating an example of a change in load reduction time accompanying an increase in the number of times of processing when processing an object to be processed in the processing unit according to the sixth embodiment of the fourth and fifth waste disposal apparatuses.
  • FIG. 10 is a graph illustrating an example of a change in current consumption of a motor with an increase in the number of times of processing when processing an object to be processed in a processing unit according to Embodiment 6 of the fourth and fifth waste processing apparatuses. It is.
  • the waste disposal apparatus 1 of Embodiment 1 of the first waste disposal apparatus is a device that crushes used disposable diapers, sanitary products, pet sand, and the like, and discharges the waste to a sewer pipe.
  • These wastes are formed of pulp, plastic, superabsorbent polymer (SAP, superabsorbent polymer, hereinafter simply referred to as polymer), and the like.
  • SAP superabsorbent polymer
  • polymer superabsorbent polymer
  • the pulp and polymer absorb and retain moisture.
  • CaCl 2 calcium chloride
  • the polymer reacted with CaCl 2 as a decomposing agent is again in an irreversible state where it cannot absorb and retain moisture.
  • the first filth disposal apparatus 1 includes an input unit 10 having an input port for inputting used paper diapers, sanitary products, and sand for pets (hereinafter, also referred to as filth D).
  • the first filth disposal apparatus 1 includes an input unit 10 having an input port for inputting used paper diapers, sanitary products, and sand for pets (hereinafter, also referred to as filth D).
  • the chute 21 includes mixer 70, discharge path 11, first opening / closing valve 12, dilution tank 30, decomposing agent introducing device 13, deodorizing apparatus 80, discharging section 14, drainage path 15, second opening / closing valve 16, separation section 40 , A first ventilation path 17, a negative pressure eliminating section 17A, a second ventilation path 18, and a third ventilation path 19.
  • the charging section 10 extends in the up-down direction, has a cylindrical shape, and is opened at an upper end to form a charging port.
  • the input port is provided with a first lid 60 that opens and closes the input port.
  • the filth D having a polymer capable of absorbing and retaining moisture is charged into the charging section 10.
  • the crushing unit 20 uses a crusher (for example, a known disposer or shredder).
  • the upper end of the crushing section 20 is connected to the lower end of the charging section 10.
  • a motor 20G for driving the crushing unit 20 is attached to a side surface of the crushing unit 20.
  • the operation of the motor 20G is controlled by a control unit (not shown).
  • the crushing unit 20 crushes the filth D input into the input unit 10 to obtain a crushed material C.
  • the control unit is configured as a control circuit including a microcomputer, for example, and has a CPU, a storage unit, and the like.
  • An operation unit (not shown) is electrically connected to the control unit, and the user of the waste disposal apparatus 1 operates the operation unit to start or end the operation of the waste disposal apparatus 1. It has a configuration that can be used.
  • a control unit is electrically connected to the motor 20G of the crushing unit 20.
  • the control unit is configured to detect the amount of power consumption consumed by the motor 20G of the crushing unit 20 and detect the first load related to the crushing unit 20 based on the detected amount of power consumption.
  • the chute 21 has a cylindrical shape formed by reducing the diameter from the upper end to the lower end, and the upper end is connected to the lower end of the crushing unit 20.
  • the chute 21 guides the crushed material C from the crushing unit 20 to a mixer 70 described later.
  • a second lid 22 is provided at a lower end of the chute 21.
  • the second lid 22 closes the lower end of the chute 21 when the crushed material C or the like is not placed.
  • the second lid 22 hangs down by the weight of the crushed material C or the like and releases the lower end of the chute 21.
  • the second lid 22 closes the lower end of the chute 21 again when the placed crushed material C or the like flows into the mixer 70.
  • the second lid 22 can prevent the later-described agitated material S from being scattered from the mixer 70 toward the crushing unit 20 and the charging unit 10 and prevent the odor from rising and rising.
  • the mixer 70 has its upper end connected to the lower end of the chute 21. On the lower surface of the mixer 70, a motor 70A for driving the mixer 70 is attached. The mixer 70 stirs the crushed material C and the decomposing agent into a stirred material S.
  • the control unit is electrically connected to the motor 70A of the mixer 70. The control unit is configured to detect the magnitude of the current consumed by the motor 70A of the mixer 70 and to detect the second load related to the mixer 70 based on the detected magnitude of the consumed current. Specifically, when the magnitude of the current consumed by the motor 70A of the mixer 70 exceeds a predetermined value during operation, it is assumed that the polymer reaction described below has not been completed.
  • the first on-off valve 12 is, for example, a known electric ball valve.
  • the first on-off valve 12 is provided at one end of the discharge path 11 and opens and closes the discharge path 11. The operation of opening and closing the first on-off valve 12 is controlled by the control unit.
  • the diluting tank 30 dilutes the agitated material S into at least one of water and hot water supplied from the discharge unit 14 described later to obtain a diluted material T.
  • the other end of the discharge path 11 is connected to the upper surface of the dilution tank 30, and the discharge path 11 communicates with the inside of the dilution tank 30.
  • the dilution tank 30 communicates with the downstream side of the crushing section 20.
  • a motor 30 ⁇ / b> A is mounted on the upper surface of the dilution tank 30.
  • a propeller (not shown) connected to the rotation shaft of the motor 30A is disposed in the dilution tank 30. The operation of the motor 30A of the dilution tank 30 is controlled by the control unit.
  • An inspection port 30 ⁇ / b> B is formed on a side surface of the dilution tank 30.
  • the inspection port 30B is closed in a watertight manner by a lid 30C.
  • the lid 30C is removed, and the inside of the dilution tank 30 is inspected from the inspection port 30B.
  • a control unit is electrically connected to the motor 30A of the dilution tank 30.
  • the control unit is configured to detect the magnitude of the current consumed by the motor 30A of the dilution tank 30, and to detect the third load related to the dilution tank 30 based on the detected magnitude of the consumed current. Specifically, it is assumed that when the magnitude of the current consumed by the motor 30A of the dilution tank 30 exceeds a predetermined value, the reaction of the polymer described later has not been completed.
  • the decomposing agent input device 13 inputs the decomposing agent into the chute 21.
  • the decomposing agent introducing device 13 is attached to a side surface of the chute 21.
  • a known feeder or the like is used as the decomposing agent introducing device 13, and the control unit controls the chute 21 to supply a predetermined amount of the decomposing agent.
  • the amount of the predetermined amount of the decomposing agent is an amount capable of uniformly extracting water from the polymer contained in the waste D.
  • the control unit of the decomposing agent charging device 13 is electrically connected.
  • the control unit supplies the decomposing agent from the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, the signal corresponding to the magnitude of the second load, and the signal corresponding to the magnitude of the third load.
  • the decomposing agent feeding device 13 is controlled so as to perform the above.
  • the deodorizing device 80 has an intake unit 80A, a deodorizing unit 80B, and a blowing unit 80C.
  • a known axial fan or the like is used for the intake section 80A.
  • the suction section 80A sucks in air from one end face and blows air from the other end face.
  • the suction unit 80A is electrically connected to the control unit.
  • the suction unit 80A is attached so as to cover a first connection port 10D, which is a connection port formed on a side surface of the input unit 10, with one end surface.
  • the intake section 80A takes in air from the input section 10.
  • a so-called deodorizing filter formed of a nonwoven fabric or the like to which activated carbon is attached is used for the deodorizing section 80B.
  • the deodorizing section 80B is arranged so as to cover the other end face (that is, the air blowing face) of the suction section 80A.
  • the blower unit 80C has the same configuration as the suction unit 80A, and for example, a known axial fan or the like is used.
  • the blowing unit 80C is electrically connected to the control unit.
  • the blowing unit 80C is attached so as to cover the second connection port 10E, which is a connection port formed on the side surface of the input unit 10, with the other end surface.
  • the charging section 10 is open to the atmosphere via a deodorizing device 80.
  • the blowing unit 80C blows air to the charging unit 10.
  • the deodorizing device 80 deodorizes the odor generated from at least one of the waste D and the crushed material C.
  • the deodorizing device 80 is connected to the first connection port 10D and the second connection port 10E.
  • the discharge unit 14 supplies at least one of water and hot water to the crushing unit 20.
  • the discharge unit 14 has a first discharge unit 14A that supplies water and a second discharge unit 14B that supplies hot water.
  • the discharge unit 14 is provided in the input unit 10.
  • a first solenoid valve 14C and a second solenoid valve 14D are provided in each of the first ejection section 14A and the second ejection section 14B.
  • the first solenoid valve 14C and the second solenoid valve 14D are controlled by the control unit to supply water or hot water to the crushing unit 20 based on predetermined conditions. Specifically, the control unit counts the elapsed time since the driving of the motor 20G of the crushing unit 20 is stopped, counts the number of times the motor 20G of the crushing unit 20 is driven, and inputs the disintegrant. It is configured to be able to count the amount of the disintegration agent or the number of times the disintegrant has been charged or to count a predetermined time.
  • control unit determines at least one of a predetermined elapsed time after the operation of the crushing unit 20 has stopped, a predetermined number of times the crushing unit 20 has operated, a predetermined amount of the disintegrant, and a predetermined number of times of the injection.
  • discharge unit 14 is controlled so as to supply at least one of water and hot water at any one of the predetermined times. Thereby, the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 can be washed.
  • the drainage channel 15 is connected at one end to the lower end of the dilution tank 30.
  • the other end of the drain 15 communicates with a sewer pipe (not shown).
  • a trap 15 ⁇ / b> A is formed in the drainage channel 15.
  • a jet drain section is connected to the trap 15A (not shown).
  • the second on-off valve 16 is, for example, a known electric ball valve.
  • the second on-off valve 16 is provided upstream of the trap 15 ⁇ / b> A of the drainage channel 15 and opens and closes the drainage channel 15. The operation of opening and closing the second on-off valve 16 is controlled by the control unit.
  • the separation unit 40 is provided in the drainage channel 15 between the trap 15A and the second on-off valve 16.
  • the separation section 40 is connected to the downstream side of the dilution tank 30.
  • As the separation unit 40 for example, a known screw press device or the like is used.
  • a motor 40C for driving the separation unit 40 is attached to a side surface of the separation unit 40.
  • a solids discharge section 40D for discharging solids separated from the diluent T is connected to the upper end of the separation section 40.
  • the separation section 40 can separate and extract solids from the diluent T flowing through the drainage channel 15.
  • the operation of the motor 40C of the separation unit 40 is controlled by the control unit.
  • An inspection port 40 ⁇ / b> A is formed on a side surface of the separation unit 40.
  • the inspection port 40A is closed in a watertight manner by a lid 40B. When inspecting the inside of the separation unit 40, the lid 40B is removed, and the inside of the separation unit 40 is inspected from
  • One end of the first ventilation path 17 communicates with the charging section 10 downstream of the first connection port 10D and the second connection port 10E, and the other end is connected to the upper end of the dilution tank 30 and communicates with the dilution tank 30. doing.
  • the negative pressure eliminating section 17A is attached to the first ventilation path 17.
  • a well-known Dolgo ventilation valve, a covert ventilation valve, or the like is used for the negative pressure eliminating section 17A.
  • One end of the second ventilation path 18 is connected to and connected to the downstream side of the negative pressure eliminating section 17A of the first ventilation path 17, and the other end is connected to and connected to the upper end of the separation section 40. Communicating.
  • the negative pressure eliminating section 17A eliminates the negative pressure in the dilution tank 30 and the separation section 40 via the first ventilation path 17 and the second ventilation path 18.
  • the third ventilation path 19 has one end connected to and connected to the side surface of the charging section 10, and the other end connected to and connected to the solids discharge section 40 ⁇ / b> D of the separation section 40.
  • An intake unit 19A is attached to the third ventilation path 19.
  • the suction unit 19A has the same configuration as the blowing unit 80C and the suction unit 80A of the deodorizing device 80, and for example, a known axial fan or the like is used.
  • the suction unit 19A is electrically connected to the control unit.
  • the suction section 19A is attached to the third ventilation path 19 so that when the suction section 19A is driven, the air in the third ventilation path 19 flows from the solids discharge section 40D toward the charging section 10.
  • the operation of the first waste disposal apparatus 1 will be described.
  • the first lid 60 is set in the upright state, the input port is opened, and the waste D is input into the input section 10.
  • the control unit starts the operation of the suction unit 80A and the blower unit 80C of the deodorization device 80.
  • the first lid 60 is placed in the lying state, the input port of the input unit 10 is closed, and the operation unit (not shown) is operated to operate the waste disposal apparatus 1.
  • the waste disposal apparatus 1 first operates at least one of the first solenoid valve 14C and the second solenoid valve 14D by the control unit to discharge at least one of the first predetermined amount of water and hot water from the discharge unit 14. It is supplied to the crushing unit 20. Thus, the filth D and at least one of water and hot water are put into the crushing unit 20. At this time, the first on-off valve 12 is in a closed state.
  • the motor 20G of the crushing unit 20 is not driven when the control unit determines that the first lid 60 has at least one of the state in which the inlet is opened and the state in which the disintegrant is not charged. It is controlled by the control unit.
  • the control unit determines that the first lid 60 is in the state in which the inlet is closed and the state in which the decomposing agent is charged, the motor 20G of the crushing unit 20 is driven, and the waste D is crushed.
  • the control unit estimates the amount of the input waste D based on the magnitude of the first load of the motor 20G. Specifically, the control unit detects the first load (that is, the power consumption of the motor 20G) related to the crushing unit 20 and crushes the waste D when the first load exceeds a predetermined value. Then, the amount of the waste D is estimated based on the time when the first load exceeds the predetermined value. The filth D is crushed in the crushing unit 20 to become the crushed material C.
  • the control unit operates the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, and injects a predetermined amount of the decomposing agent into the chute 21.
  • a predetermined amount of the decomposing agent supplied to the chute 21 flows into the mixer 70.
  • the crushed material C, at least one of the first predetermined amount of water and hot water, and the predetermined amount of the decomposing agent are stirred, and the polymer having absorbed and retained the water and the decomposing agent are mixed.
  • the reaction is allowed to take out the water absorbed and retained by the polymer.
  • the crushed material C, at least one of water and hot water, and a predetermined amount of the decomposing agent are stirred to form the stirred material S.
  • the controller detects the second load related to the motor 70A of the mixer 70. Specifically, the magnitude of the second load detected at this time is the magnitude of the current consumption of the motor 70A.
  • the control unit determines that the magnitude of the second load of the motor 70A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the agitated material S and the decomposer has not sufficiently proceeded)
  • the disintegrating agent injecting device 13 is controlled so that an agent is additionally injected from the injecting agent injecting device 13.
  • the motor 70A is continuously driven, and the mixer 70 can further promote the reaction between the polymer of the agitated substance S and the decomposing agent.
  • the crushed material C, at least one of the first predetermined amount of water and hot water, and the decomposing agent are agitated, and the crushed material C is converted into the agitated material S.
  • the reaction with can be further advanced.
  • the control unit determines that the magnitude of the current consumption of the motor 70A (that is, the magnitude of the second load) is equal to or smaller than a predetermined value
  • the first on-off valve 12 in the closed state is opened by the control unit. To be. Then, the agitated material S flows into the dilution tank 30 via the discharge path 11.
  • the first electromagnetic valve 14C and the second electromagnetic valve 14D of the discharge unit 14 are operated by the control unit to supply at least one of the second predetermined amount of water and hot water from the discharge unit 14 to the crushing unit 20.
  • At least one of the second predetermined amount of water and hot water is a predetermined amount with respect to the amount of the stirring object S.
  • the motor 20G of the crushing unit 20 and the motor 70A of the mixer 70 are being driven.
  • the inside of the crushing unit 20 and the inside of the mixer 70 can be washed while the stirred material S in the mixer 70 is surely conveyed into the dilution tank 30.
  • the first ventilation path 17 suppresses the inside of the dilution tank 30 from becoming a positive pressure when at least one of the crushed material C and the second predetermined amount of water and hot water flows into the dilution tank 30. If at least one of the water and the hot water overflows from the crushing unit 20 when at least one of the second predetermined amount of the water and the hot water is supplied from the discharge unit 14, the second predetermined amount is supplied through the first ventilation path 17. 2 A part of at least one of the predetermined amount of water and hot water flows into the dilution tank 30.
  • the second on-off valve 16 is in a closed state when at least one of the second predetermined amount of water and hot water and the agitated material S flow into the dilution tank 30.
  • the second predetermined amount of water and hot water and the stirred material S are diluted in the dilution tank 30 to make the stirred material S a diluted material T.
  • the second on-off valve 16 is in a closed state.
  • the drive of the motor 30A of the dilution tank 30 is started by the control unit.
  • the propeller (not shown) of the dilution tank 30 rotates, and the second predetermined amount of at least one of water and hot water and the agitated material S are agitated. Become.
  • the concentration of Ca (calcium) or Cl (chlorine) of the decomposing agent contained in the agitated material S in the agitated material S can be reduced by using the diluent T, and the Ca component adheres to the sewer pipe. It is possible to suppress that the sewer pipe is corroded due to hardening or Cl.
  • the third load on the motor 30A of the dilution tank 30 is monitored by the control unit. Specifically, the magnitude of the third load detected at this time is the magnitude of the current consumption of the motor 30A of the dilution tank 30.
  • control unit determines that the magnitude of the third load of the motor 30A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the diluent T and the decomposer has not sufficiently proceeded)
  • the decomposing agent input device 13 is controlled so that the decomposing agent is additionally input from the decomposing agent input device 13.
  • the motor 30A of the dilution tank 30 is also continuously driven, and the reaction between the polymer of the diluent T and the decomposing agent can be further advanced in the dilution tank 30.
  • the agitated material S and at least one of the second predetermined amount of water and hot water are agitated, and the agitated material S is diluted to the diluted material T in which the reaction between the polymer and the decomposing agent has progressed.
  • a configuration may be adopted in which a decomposing agent inlet is formed in the dilution tank 30 and a decomposing agent can be supplied from the decomposing agent input device 13 also to this decomposing agent inlet.
  • the decomposing agent can be directly injected into the dilution tank 30.
  • the solid content is separated from the diluent T.
  • the control unit determines that the magnitude of the current consumption of the motor 30A (that is, the magnitude of the third load) is equal to or smaller than a predetermined value, the control unit causes the second on-off valve 16 in the closed state to be closed. It is left open. Then, the diluent T flows from the dilution tank 30 toward the separation unit 40.
  • the input port of the waste disposal apparatus 1 is closed by the first lid 60. For this reason, by taking in air from the negative pressure eliminating portion 17A of the first ventilation path 17 into the first ventilation path 17, it is possible to prevent the inside of the dilution tank 30 from becoming a negative pressure. , And can be satisfactorily flowed toward the separation section 40.
  • the drive of the motor 40C of the separation unit 40 is started by the control unit. At this time, the operation of the suction unit 19A is also started by the control unit.
  • the diluent T that has flowed into the drainage channel 15 flows into the separation unit 40, and the solid content of the diluent T is discharged from the solid discharge unit 40D by driving the motor 40C.
  • the solids of the diluent T discharged from the solids discharge unit 40D are taken into the collection bag 40E attached to the tip of the solids discharge unit 40D.
  • the odor generated in the solids discharge section 40D is guided to the input section 10 by the third ventilation path 19 and the suction section 19A.
  • the water of the diluent T flows through the trap 15A to a drain (not shown).
  • the separating section 40 is in communication with the first ventilation path 17 via the second ventilation path 18. Thereby, the inside of the separation unit 40 is suppressed from being negative pressure, and the water of the diluent T can be satisfactorily flowed from the separation unit 40 toward the sewer pipe.
  • the water of the diluent T remaining in the trap 15A is surely conveyed to the sewer pipe by vigorously supplying water to the trap 15A from a jet drain (not shown) connected to the trap 15A.
  • the motors 20G, 70A, 30A of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are operated. , 40C are stopped.
  • the control unit controls so that hot water is supplied from the second discharge unit 14B of the discharge unit 14.
  • the motors 20G, 70A, 30A, and 40C of the crushing unit 20 the mixer 70, the dilution tank 30, and the separation unit 40 are driven by the control unit, and the first on-off valve 12 and the second on-off valve 16 are opened.
  • the waste disposal apparatus 1 is cleaned so that the waste D, the crushed substance C, the agitated substance S, the diluent T, and the like do not remain in the waste disposal apparatus 1, and the Ca component is contained in the waste disposal apparatus 1. It is possible to suppress adhesion and solidification, and corrosion of the inside of the waste disposal apparatus 1 by Cl.
  • the first filth disposal apparatus 1 can crush the filth D in the crushing unit 20 to obtain the crushed material C.
  • the odor rising from at least one of the waste material D and the crushed material C can be deodorized by the deodorizing device 80.
  • the first waste disposal apparatus 1 can suppress the rise of odor in the room.
  • the first waste disposal apparatus 1 communicates with the downstream side of the crushing unit 20, and a dilution tank 30 that dilutes the crushed material C with water to make a diluted material T, and has one end having a first connection port 10D and a second connection port 10E. And a first ventilation path 17 connected to the dilution tank 30 at the other end.
  • the dilution tank 30 suppresses a negative pressure when the diluent T is discharged to the downstream side, and suppresses a positive pressure when the crushed material C or the like flows into the dilution tank 30. It is possible to improve the inflow of the crushed material C and the like and the discharge of the diluted material T.
  • the first waste disposal apparatus 1 is connected to the downstream side of the dilution tank 30, and has a separation unit 40 that separates solids from the diluent T, one end connected to the first ventilation path 17, and the other end connected to the separation unit 40. And a second air passage 18 connected thereto.
  • the separation unit 40 can suppress the negative pressure when discharging the moisture from which the solid content has been removed from the diluent T to the downstream side, and can desirably remove the moisture from which the solid content has been removed from the diluent T. Can be discharged.
  • the first waste disposal apparatus 1 includes a first lid 60 for closing the charging section 10 and a negative pressure eliminating section 17A for eliminating negative pressure in the dilution tank 30 and the separating section 40. For this reason, by closing the charging section 10 with the first lid 60, the dilution tank 30 and the separation section 40 are likely to have a negative pressure when discharging the diluent T or water obtained by removing solids from the diluent T. Become. However, the negative pressure eliminating section 17A can prevent the dilution tank 30 and the separating section 40 from becoming negative pressure even when the charging section 10 is closed with the first lid 60.
  • the separation unit 40 of the first waste disposal apparatus 1 has a solids discharge unit 40D for discharging solids separated from the diluent T, one end of which is connected to the input unit 10 and the other end of which is a solids discharge unit 40D. Is provided with a third ventilation path 19 connected to the third air passage. Therefore, the odor generated in the solids discharge section 40D can be guided to the input section 10 and the input section 10 can be deodorized by the deodorizing device 80.
  • the deodorizing device 80 of the first waste disposal apparatus 1 has an intake unit 80A that takes in air from the charging unit 10 and a blowing unit 80C that blows air to the charging unit 10. Therefore, by circulating the air in the charging section 10 between the suction section 80A and the blowing section 80C in the charging section 10, it is possible to satisfactorily deodorize.
  • the first embodiment of the waste disposal apparatus 2 according to the second embodiment is different from the first embodiment in the form of a deodorizing apparatus 180.
  • the same components as those in the first embodiment are denoted by the same reference numerals, and detailed description thereof will be omitted.
  • the deodorizing device 180 for example, a known sprayer or the like is used.
  • the deodorizing device 180 has a deodorant spraying section 180F for storing a deodorant 180D for eliminating odors, and a fragrance spraying section 180G for storing a fragrance 180E that generates fragrance.
  • the deodorizing device 180 is electrically connected to the control unit.
  • the deodorant spraying section 180F is arranged such that a spray port for spraying the stored deodorant 180D communicates with the second connection port 10E.
  • the fragrance spraying section 180G is arranged such that a spray port for spraying the stored fragrance 180E communicates with the first connection port 10D.
  • the deodorizing device 180 sprays the deodorant 180D and the fragrance 180E stored by the control unit toward the charging unit 10 based on, for example, the first lid 60 being in the upright state.
  • the first filth disposal apparatus 2 can crush the filth D in the crushing unit 20 to obtain the crushed material C.
  • the odor rising from at least one of the waste material D and the crushed material C can be deodorized by the deodorizing device 180.
  • the first waste disposal apparatus 2 can also suppress the rise of odor in the room.
  • the deodorizing device 180 of the first waste disposal device 2 has a deodorant 180D for eliminating odors and a fragrance 180E for generating fragrance. For this reason, the odor can be satisfactorily suppressed in the charging section 10.
  • the waste disposal apparatus 3 according to the third embodiment of the first waste disposal apparatus is different from the first and second embodiments in the form of the charging unit 110 and the form of the first lid 160.
  • the same components as those in the first and second embodiments are denoted by the same reference numerals, and detailed description thereof will be omitted.
  • a water sealing section 110A is provided at the upper end of the charging section 110.
  • the water seal portion 110A has a bottom portion 110B extending in an annular shape from the inner peripheral surface of the charging portion 110 to the inside, and an upright wall portion 110C that rises cylindrically upward from an inner end of the bottom portion 110B.
  • a storage section P in which water is stored is formed in a region surrounded by an inner peripheral surface of the input section 110, a bottom section 110B, and an upright wall section 110C.
  • the first lid 160 has a flat plate shape, and has a grip portion 160A at the center.
  • the first lid 160 is provided with a hanging wall 160B which hangs from an outer peripheral end.
  • the first lid 160 is placed on the water seal portion 110A such that the lower side of the hanging wall 160B is immersed in the storage portion P.
  • the first filth disposal apparatus 3 can crush the filth D in the crushing unit 20 to obtain the crushed material C.
  • the odor rising from at least one of the waste material D and the crushed material C can be deodorized by the deodorizing device 180.
  • the first filth disposal device 3 can also suppress the rise of odor in the room.
  • the waste disposal apparatus 4 of Embodiment 4 of the second waste disposal apparatus is an apparatus for crushing used paper diapers, sanitary products, and the like, which are waste, and discharging the waste to a sewer pipe.
  • These wastes are formed of pulp, plastic, superabsorbent polymer (SAP, superabsorbent polymer, hereinafter simply referred to as polymer), and the like.
  • SAP superabsorbent polymer
  • polymer superabsorbent polymer
  • the pulp and the polymer absorb and retain moisture.
  • CaCl 2 calcium chloride
  • CaCl 2 calcium chloride
  • the polymer reacted with CaCl 2 as a decomposing agent is again in an irreversible state where it cannot absorb and retain moisture.
  • a disposable diaper has a front sheet and a back sheet fixed by hot melt or the like. Further, a pad-type disposable diaper is generally provided with an adhesive tape used for attaching to underwear or the like. It is known that hot melts and pressure-sensitive adhesive tapes are softened when heated to 40 ° C. or higher, and have low adhesive strength.
  • the waste disposal apparatus 4 includes an input section 10 in which an input port for inputting used paper diapers and sanitary articles (hereinafter, also referred to as waste D) is formed, a crushing section 20, a chute 21, and a mixer 70. , Discharge path 11, first opening / closing valve 12, dilution tank 30, decomposing agent introducing device 13, deodorizing device 80, discharge section 14, drainage path 15, second opening / closing valve 16, separating section 40, first ventilation path 17, negative A pressure relief section 17A, a second ventilation path 18, and a third ventilation path 19 are provided.
  • Each of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 is a processing unit that separates the waste D having a polymer capable of absorbing and retaining moisture.
  • the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are also referred to as all processing units.
  • the waste disposal apparatus 4 can selectively execute a treatment mode for treating the waste D and a washing mode for washing the input unit 10 and all the treatment units.
  • the charging section 10 extends in the up-down direction, has a cylindrical shape, and is opened at an upper end to form a charging port.
  • the input port is provided with a first lid 60 for opening and closing the input port.
  • the filth D having a polymer capable of absorbing and retaining moisture is charged into the charging section 10.
  • the crushing unit 20 uses a crusher (for example, a known disposer or shredder).
  • the upper end of the crushing section 20 is connected to the lower end of the charging section 10.
  • a motor 20G for driving the crushing unit 20 and a heater H1 are attached to a side surface of the crushing unit 20.
  • the operation of the motor 20G is controlled by a control unit (not shown).
  • the operation of the heater H1 is controlled by the control unit.
  • the crushing unit 20 crushes the filth D input into the input unit 10 to obtain a crushed material C.
  • the control unit is configured as a control circuit including a microcomputer, for example, and has a CPU, a storage unit, and the like.
  • An operation unit (not shown) is electrically connected to the control unit. When a user using the waste disposal apparatus 4 operates the operation unit, the operation of the waste disposal apparatus 4 is started or terminated. It has a configuration that can be used.
  • a control unit is electrically connected to the motor 20G of the crushing unit 20.
  • the control unit is configured to detect the amount of power consumption consumed by the motor 20G of the crushing unit 20 and detect the first load related to the crushing unit 20 based on the detected amount of power consumption.
  • the chute 21 has a cylindrical shape formed by reducing the diameter from the upper end to the lower end, and the upper end is connected to the lower end of the crushing unit 20.
  • the chute 21 guides the crushed material C from the crushing unit 20 to a mixer 70 described later.
  • a second lid 22 is provided at a lower end of the chute 21.
  • the second lid 22 closes the lower end of the chute 21 when the crushed material C or the like is not placed.
  • the second lid 22 hangs down by the weight of the crushed material C or the like and releases the lower end of the chute 21.
  • the second lid 22 closes the lower end of the chute 21 again when the placed crushed material C or the like flows into the mixer 70.
  • the second lid 22 can prevent the later-described agitated material S from being scattered from the mixer 70 toward the crushing unit 20 and the charging unit 10 and prevent the odor from rising and rising.
  • a heater H2 is attached to a side surface of the chute 21. The operation of the heater H2 is controlled by the control unit.
  • the mixer 70 has its upper end connected to the lower end of the chute 21. On the lower surface of the mixer 70, a motor 70A for driving the mixer 70 is attached. The mixer 70 stirs the crushed material C and the decomposing agent into a stirred material S.
  • the control unit is electrically connected to the motor 70A of the mixer 70. The control unit is configured to detect the magnitude of the current consumed by the motor 70A of the mixer 70 and to detect the second load related to the mixer 70 based on the detected magnitude of the consumed current. Specifically, when the magnitude of the current consumed by the motor 70A of the mixer 70 exceeds a predetermined value during operation, it is assumed that the polymer reaction described below has not been completed.
  • a heater H2 is attached to a side surface of the mixer 70. The operation of the heater H2 is controlled by the control unit.
  • the first on-off valve 12 is, for example, a known electric ball valve.
  • the first on-off valve 12 is provided at one end of the discharge path 11 and opens and closes the discharge path 11. The operation of opening and closing the first on-off valve 12 is controlled by the control unit.
  • the diluting tank 30 dilutes the agitated material S into at least one of water and hot water supplied from the discharge unit 14 described later to obtain a diluted material T.
  • the other end of the discharge path 11 is connected to the upper surface of the dilution tank 30, and the discharge path 11 communicates with the inside of the dilution tank 30.
  • the dilution tank 30 communicates with the downstream side of the crushing section 20.
  • a motor 30 ⁇ / b> A is mounted on the upper surface of the dilution tank 30.
  • a propeller (not shown) connected to the rotation shaft of the motor 30A is disposed in the dilution tank 30. The operation of the motor 30A of the dilution tank 30 is controlled by the control unit.
  • An inspection port 30 ⁇ / b> B is formed on a side surface of the dilution tank 30.
  • the inspection port 30B is closed in a watertight manner by a lid 30C.
  • the lid 30C is removed, and the inside of the dilution tank 30 is inspected from the inspection port 30B.
  • a control unit is electrically connected to the motor 30A of the dilution tank 30.
  • the control unit is configured to detect the magnitude of the current consumed by the motor 30A of the dilution tank 30, and to detect the third load related to the dilution tank 30 based on the detected magnitude of the consumed current. Specifically, it is assumed that when the magnitude of the current consumed by the motor 30A of the dilution tank 30 exceeds a predetermined value, the reaction of the polymer described later has not been completed.
  • a heater H3 is attached to a side surface of the dilution tank 30. The operation of the heater H3 is controlled by the control unit.
  • the decomposing agent input device 13 inputs the decomposing agent into the chute 21.
  • the decomposing agent introducing device 13 is attached to a side surface of the chute 21.
  • a known feeder or the like is used as the decomposing agent introducing device 13, and the control unit controls the chute 21 to supply a predetermined amount of the decomposing agent.
  • the amount of the predetermined amount of the decomposing agent is an amount capable of uniformly extracting water from the polymer contained in the waste D.
  • the control unit of the decomposing agent charging device 13 is electrically connected.
  • the control unit supplies the decomposing agent from the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, the signal corresponding to the magnitude of the second load, and the signal corresponding to the magnitude of the third load.
  • the decomposing agent feeding device 13 is controlled so as to perform the above.
  • the deodorizing device 80 has an intake unit 80A, a deodorizing unit 80B, and a blowing unit 80C.
  • a known axial fan or the like is used for the intake section 80A.
  • the suction section 80A sucks in air from one end face and blows air from the other end face.
  • the suction unit 80A is electrically connected to the control unit.
  • the suction unit 80A is attached so as to cover the first connection port 10D formed on the side surface of the insertion unit 10 with one end surface.
  • the intake section 80A takes in air from the input section 10.
  • a so-called deodorizing filter formed of a nonwoven fabric or the like to which activated carbon is attached is used for the deodorizing section 80B.
  • the deodorizing section 80B is arranged so as to cover the other end face (that is, the air blowing face) of the suction section 80A.
  • the blower unit 80C has the same configuration as the suction unit 80A, and for example, a known axial fan or the like is used.
  • the blowing unit 80C is electrically connected to the control unit.
  • the blowing unit 80C is attached so as to cover the second connection port 10E formed on the side surface of the charging unit 10 with the other end surface.
  • the charging section 10 is open to the atmosphere via a deodorizing device 80.
  • the blowing unit 80C blows air to the charging unit 10.
  • the deodorizing device 80 deodorizes the odor generated from at least one of the waste D and the crushed material C.
  • the deodorizing device 80 is connected to the first connection port 10D and the second connection port 10E.
  • the discharge unit 14 supplies at least one of water and hot water to the crushing unit 20.
  • the discharge unit 14 has a first discharge unit 14A that supplies water and a second discharge unit 14B that supplies hot water.
  • the discharge unit 14 is provided in the input unit 10.
  • a first solenoid valve 14C and a second solenoid valve 14D are provided in each of the first ejection section 14A and the second ejection section 14B.
  • the temperature of the hot water discharged from the second discharge portion 14B is 40 ° C to 90 ° C.
  • the first solenoid valve 14C and the second solenoid valve 14D are controlled by the control unit to supply water or hot water to the crushing unit 20 based on predetermined conditions in the cleaning mode for cleaning all the processing units. .
  • the control unit counts the elapsed time since the driving of the motor 20G of the crushing unit 20 is stopped, counts the number of times the motor 20G of the crushing unit 20 is driven, and inputs the disintegrant. It is configured to be able to count the amount of the disintegration agent or the number of times the disintegrant has been charged or to count a predetermined time.
  • the waste disposal apparatus 4 performs the predetermined time elapsed after the operation of the crushing section 20 has stopped, the predetermined number of times the crushing section 20 has operated, and the predetermined amount of the decomposing agent.
  • the control unit controls the discharge unit 14 to supply at least one of water and hot water for at least one of the charging amount and the predetermined number of charging times and for the predetermined time period.
  • the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 can be washed. That is, the discharge unit 14 periodically discharges at least one of water and hot water to clean all the processing units.
  • the drainage channel 15 is connected at one end to the lower end of the dilution tank 30.
  • the other end of the drain 15 communicates with a sewer pipe (not shown).
  • a trap 15 ⁇ / b> A is formed in the drainage channel 15.
  • a jet drain section is connected to the trap 15A (not shown).
  • the second on-off valve 16 is, for example, a known electric ball valve.
  • the second on-off valve 16 is provided upstream of the trap 15 ⁇ / b> A of the drainage channel 15 and opens and closes the drainage channel 15. The operation of opening and closing the second on-off valve 16 is controlled by the control unit.
  • the separation unit 40 is provided in the drainage channel 15 between the trap 15A and the second on-off valve 16.
  • the separation section 40 is connected to the downstream side of the dilution tank 30.
  • As the separation unit 40 for example, a known screw press device or the like is used.
  • a motor 40C for driving the separation unit 40 is attached to a side surface of the separation unit 40.
  • a solids discharge section 40D for discharging solids separated from the diluent T is connected to the upper end of the separation section 40.
  • the separation section 40 can separate and extract solids from the diluent T flowing through the drainage channel 15.
  • the operation of the motor 40C of the separation unit 40 is controlled by the control unit.
  • An inspection port 40 ⁇ / b> A is formed on a side surface of the separation unit 40.
  • the inspection port 40A is closed in a watertight manner by a lid 40B.
  • the lid 40B is removed, and the inside of the separation unit 40 is inspected from the inspection port 40A.
  • a heater H4 is attached to a side surface of the separation unit 40. The operation of the heater H4 is controlled by the control unit.
  • the second on-off valve 16 is provided between the dilution tank 30 and the separation unit 40, and is provided between two downstream processing units (the dilution tank 30 and the separation unit 40) among all the processing units. Have been.
  • One end of the first ventilation path 17 communicates with the charging section 10 downstream of the first connection port 10D and the second connection port 10E, and the other end is connected to the upper end of the dilution tank 30 and communicates with the dilution tank 30. doing.
  • the negative pressure eliminating section 17A is attached to the first ventilation path 17.
  • a well-known Dolgo ventilation valve, a covert ventilation valve, or the like is used for the negative pressure eliminating section 17A.
  • One end of the second ventilation path 18 is connected to and connected to the downstream side of the negative pressure eliminating section 17A of the first ventilation path 17, and the other end is connected to and connected to the upper end of the separation section 40. Communicating.
  • the negative pressure eliminating section 17A eliminates the negative pressure in the dilution tank 30 and the separation section 40 via the first ventilation path 17 and the second ventilation path 18.
  • the third ventilation path 19 has one end connected to and connected to the side surface of the charging section 10, and the other end connected to and connected to the solids discharge section 40 ⁇ / b> D of the separation section 40.
  • An intake unit 19A is attached to the third ventilation path 19.
  • the suction unit 19A has the same configuration as the blowing unit 80C and the suction unit 80A of the deodorizing device 80, and for example, a known axial fan or the like is used.
  • the suction unit 19A is electrically connected to the control unit.
  • the suction section 19A is attached to the third ventilation path 19 so that when the suction section 19A is driven, the air in the third ventilation path 19 flows from the solids discharge section 40D toward the charging section 10.
  • the operation in the processing mode in which the waste disposal apparatus 4 separates the waste D will be described.
  • the first lid 60 is set in the upright state, the input port is opened, and the waste D is input into the input section 10.
  • the control unit starts the operation of the suction unit 80A and the blower unit 80C of the deodorization device 80.
  • the first lid 60 is placed in the lying state, the input port of the input section 10 is closed, and the operation section (not shown) is operated to operate the waste disposal apparatus 4.
  • the waste disposal device 4 first operates at least one of the first solenoid valve 14C and the second solenoid valve 14D by the control unit to remove at least one of the first predetermined amount of water and hot water from the discharge unit 14. It is supplied to the crushing unit 20. Thus, the filth D and at least one of water and hot water are put into the crushing unit 20. At this time, the first on-off valve 12 is in a closed state.
  • the motor 20G of the crushing unit 20 is not driven when the control unit determines that the first lid 60 has at least one of the state in which the inlet is opened and the state in which the disintegrant is not charged. It is controlled by the control unit.
  • the control unit determines that the first lid 60 is in the state in which the inlet is closed and the state in which the decomposing agent is charged, the motor 20G of the crushing unit 20 is driven, and the waste D is crushed.
  • the control unit estimates the amount of the input waste D based on the magnitude of the first load of the motor 20G. Specifically, the control unit detects the first load (that is, the power consumption of the motor 20G) related to the crushing unit 20 and crushes the waste D when the first load exceeds a predetermined value. Then, the amount of the waste D is estimated based on the time when the first load exceeds the predetermined value. The filth D is crushed in the crushing unit 20 to become the crushed material C.
  • the control unit operates the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, and injects a predetermined amount of the decomposing agent into the chute 21.
  • the decomposing agent charged into the chute 21 flows into the mixer 70.
  • the crushed material C, at least one of the first predetermined amount of water and hot water, and the decomposing agent are stirred, and the polymer that has absorbed and held the water and the decomposing agent are reacted, The water absorbed by the polymer is taken out.
  • the crushed material C, at least one of water and hot water, and the decomposing agent are agitated into the agitated material S.
  • the controller detects the second load related to the motor 70A of the mixer 70. Specifically, the magnitude of the second load detected at this time is the magnitude of the current consumption of the motor 70A.
  • control unit determines that the magnitude of the second load of the motor 70A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the agitated product S and the decomposing agent has not sufficiently proceeded)
  • the control unit decomposes.
  • the disintegrating agent injecting device 13 is controlled so that an agent is additionally injected from the injecting agent injecting device 13.
  • the motor 70A is continuously driven, and the mixer 70 can further promote the reaction between the polymer of the agitated substance S and the decomposing agent.
  • the crushed material C, at least one of the first predetermined amount of water and hot water, and the decomposing agent are stirred, and the crushed material C is converted into the agitated material S, and the polymer of the agitated material S is decomposed.
  • the reaction with the agent can proceed further.
  • the control unit determines that the magnitude of the current consumption of the motor 70A (that is, the magnitude of the second load) is equal to or smaller than a predetermined value
  • the first on-off valve 12 in the closed state is opened by the control unit. To be. Then, the agitated material S flows into the dilution tank 30 via the discharge path 11.
  • the first electromagnetic valve 14C and the second electromagnetic valve 14D of the discharge unit 14 are operated by the control unit to supply at least one of the second predetermined amount of water and hot water from the discharge unit 14 to the crushing unit 20.
  • At least one of the second predetermined amount of water and hot water is a predetermined amount with respect to the amount of the stirring object S.
  • the motor 20G of the crushing unit 20 and the motor 70A of the mixer 70 are being driven.
  • the inside of the crushing unit 20 and the inside of the mixer 70 can be washed while the stirred material S in the mixer 70 is surely conveyed into the dilution tank 30.
  • the first ventilation path 17 suppresses the inside of the dilution tank 30 from becoming a positive pressure when at least one of the crushed material C and the second predetermined amount of water and hot water flows into the dilution tank 30.
  • the second on-off valve 16 is in a closed state when at least one of the second predetermined amount of water and hot water and the agitated material S flow into the dilution tank 30.
  • the second predetermined amount of water and hot water and the stirred material S are diluted in the dilution tank 30 to make the stirred material S a diluted material T.
  • the second on-off valve 16 is in a closed state.
  • the drive of the motor 30A of the dilution tank 30 is started by the control unit.
  • the propeller (not shown) of the dilution tank 30 rotates, and the second predetermined amount of at least one of water and hot water and the agitated material S are agitated. Become.
  • the concentration of Ca (calcium) or Cl (chlorine) of the decomposing agent contained in the agitated material S in the agitated material S can be reduced by using the diluent T, and the Ca component adheres to the sewer pipe. It is possible to suppress that the sewer pipe is corroded due to hardening or Cl.
  • the third load on the motor 30A of the dilution tank 30 is monitored by the control unit. Specifically, the magnitude of the third load detected at this time is the magnitude of the current consumption of the motor 30A of the dilution tank 30.
  • control unit determines that the magnitude of the third load of the motor 30A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the diluent T and the decomposer has not sufficiently proceeded)
  • the decomposing agent input device 13 is controlled so that the decomposing agent is additionally input from the decomposing agent input device 13.
  • the motor 30A of the dilution tank 30 is also continuously driven, and the reaction between the polymer of the diluent T and the decomposing agent can be further advanced in the dilution tank 30.
  • the agitated material S and at least one of the second predetermined amount of water and hot water are agitated, and the agitated material S is diluted to the diluted material T in which the reaction between the polymer and the decomposing agent has progressed.
  • a configuration may be adopted in which a decomposing agent inlet is formed in the dilution tank 30 and a decomposing agent can be supplied from the decomposing agent input device 13 also to this decomposing agent inlet.
  • the decomposing agent can be directly injected into the dilution tank 30.
  • the solid content is separated from the diluent T.
  • the control unit determines that the magnitude of the current consumption of the motor 30A (that is, the magnitude of the third load) is equal to or smaller than a predetermined value, the control unit causes the second on-off valve 16 in the closed state to be closed. It is left open. Then, the diluent T flows from the dilution tank 30 toward the separation unit 40.
  • the input port of the waste disposal apparatus 4 is closed by the first lid 60. For this reason, by taking in air from the negative pressure eliminating portion 17A of the first ventilation path 17 into the first ventilation path 17, it is possible to prevent the inside of the dilution tank 30 from becoming a negative pressure. , And can be satisfactorily flowed toward the separation section 40.
  • the drive of the motor 40C of the separation unit 40 is started by the control unit. At this time, the operation of the suction unit 19A is also started by the control unit.
  • the diluent T that has flowed into the drainage channel 15 flows into the separation unit 40, and the solid content of the diluent T is discharged from the solid discharge unit 40D by driving the motor 40C.
  • the solids of the diluent T discharged from the solids discharge unit 40D are taken into the collection bag 40E attached to the tip of the solids discharge unit 40D.
  • the odor generated in the solids discharge section 40D is guided to the input section 10 by the third ventilation path 19 and the suction section 19A.
  • the water of the diluent T flows through the trap 15A to a drain (not shown).
  • the separating section 40 is in communication with the first ventilation path 17 via the second ventilation path 18. Thereby, the inside of the separation unit 40 is suppressed from being negative pressure, and the water of the diluent T can be satisfactorily flowed from the separation unit 40 toward the sewer pipe.
  • the water of the diluent T remaining in the trap 15A is reliably transported to the sewer pipe by vigorously supplying water to the trap 15A from a jet drain (not shown) connected to the trap 15A.
  • the control unit controls so that hot water is supplied from the second discharge unit 14B of the discharge unit 14.
  • the discharge unit 14 discharges hot water to the charging unit 10 in the cleaning mode.
  • the control unit drives the motors 20G, 70A, 30A, and 40C to open the first on-off valve 12 and close the second on-off valve 16 of the waste disposal apparatus 4. That is, in the cleaning mode, the waste disposal device 4 discharges hot water from the discharge unit 14 while driving all the processing units.
  • the waste disposal apparatus 4 closes the second on-off valve 16 in the cleaning mode and supplies hot water to the crushing unit 20, the mixer 70, and the dilution tank 30 (hereinafter, also referred to as a processing unit excluding the separation unit 40). To store.
  • the control unit drives the motors 20G, 70A, 30A alternately in the forward and reverse directions.
  • the stored hot water flows so as to be stirred in the processing unit excluding the separation unit 40, so that the crushed material C, the agitated material S, and The hot melt and the adhesive tape contained in the diluent T are softened and the adhesive strength is reduced, and the hot melt and the adhesive tape are easily peeled off from the inner surface of the processing section excluding the separation section 40.
  • the waste disposal apparatus 4 operates the heaters H1, H2, H3 provided in each of the processing units except for the separation unit 40 to heat the hot water stored in the processing units except for the separation unit 40. Thereby, the hot melt or the adhesive tape adhered to the inner surface of the processing unit excluding the separation unit 40 is further softened to reduce the adhesive force, and the hot melt or the adhesive tape is further removed from the inner surface of the processing unit excluding the separation unit 40. Can be peeled off satisfactorily.
  • the waste treatment apparatus 4 is configured such that hot water at 62 ° C. to 65 ° C. is supplied for 30 minutes or more, and hot water at 72 ° C. to 87 ° C. is used for 15 seconds or more in the processing unit excluding the separation unit 40.
  • hot water at 72 ° C. to 87 ° C. is used for 15 seconds or more in the processing unit excluding the separation unit 40.
  • the waste disposal apparatus 4 opens the second on-off valve 16 in the closed state, and operates the heater H4. Then, together with the hot water stored in the processing unit excluding the separation unit 40, the crushed material C including the hot melt and the adhesive tape adhered to the inner surface of the processing unit excluding the separation unit 40, the agitated material S, and the diluent T flows into the separation unit 40.
  • the separation unit 40 includes solids of the crushed material C, the agitated material S, and the diluent T containing the hot melt and the adhesive tape adhered to the inner surface of the processing unit excluding the separation unit 40 (the processing excluding the separation unit 40). (Including hot melt and adhesive tape attached to the inner surface of the solid portion), and the separated solid is discharged from the solid discharge portion 40D.
  • the hot melt or the adhesive tape contained in the diluent T adhered to the inner surface of the separation unit 40 is softened by the hot water stored in the processing unit excluding the separation unit 40 and the adhesive strength is reduced. Becomes smaller.
  • the solid content of the diluent T including the hot melt and the adhesive tape adhered to the inner surface of the separation unit 40 (including the hot melt and the adhesive tape adhered to the inner surface of the separation unit 40) is also reduced. And is discharged from the solids discharge section 40D.
  • the hot water at 62 ° C. to 65 ° C. is continuously fed into the separation unit 40 for at least 30 minutes and the hot water at 72 ° C. to 87 ° C. for 15 seconds or more.
  • the second filth disposal apparatus 4 discharges hot water from the discharge unit 14 to the charging unit 10 in the cleaning mode, so that the crushed material C, the stirred material S, and the dilution remaining in all the processing units are discharged.
  • the object T can be washed out and all the processing units can be put in a good state.
  • the second waste disposal apparatus 4 can operate well.
  • the temperature of the hot water in the second waste disposal apparatus 4 is 40 ° C to 90 ° C. Therefore, the hot melt or the adhesive tape contained in the waste D is softened to reduce the adhesive strength, the hot melt or the adhesive tape is easily peeled from the inner surface of all the processing units, and the sterilization in all the processing units is performed. Can be.
  • the second waste disposal apparatus 4 includes a second on-off valve 16 between two downstream processing units of all the processing units, and closes the second on-off valve 16 in the cleaning mode to disconnect the separation unit 40. Store the hot water in the removed processing unit. For this reason, the waste disposal apparatus 4 can satisfactorily clean the inside of the processing unit excluding the separation unit 40 by storing hot water in the processing unit excluding the separation unit 40.
  • the second waste disposal apparatus 4 discharges hot water from the discharge unit 14 while driving all the processing units in the cleaning mode. Therefore, the waste disposal apparatus 4 can flow in such a manner that the hot water is stirred in all the processing sections, so that the inside of all the processing sections can be more appropriately cleaned.
  • the second waste disposal apparatus 4 includes heaters H1, H2, H3, and H4 that are provided in all processing units and heat at least one of water and hot water in all processing units. For this reason, in all the processing units, hot melt or adhesive contained in the crushed material C, the agitated material S, and the dilute material T is generated by at least one of water and hot water heated by the heaters H1, H2, H3, and H4.
  • the tape can be softened to reduce the adhesive strength, the hot melt or the adhesive tape can be easily peeled off from the inner surface of all the processing sections, and the sterilization in all the processing sections can be performed.
  • the waste disposal apparatus 5 of Embodiment 3 of the third waste disposal apparatus is an apparatus for crushing used paper diapers, sanitary products, pet sand, and the like, which are waste, and discharging the waste to a sewer pipe.
  • These wastes are formed of pulp, plastic, superabsorbent polymer (SAP, superabsorbent polymer, hereinafter simply referred to as polymer), and the like.
  • SAP superabsorbent polymer
  • polymer superabsorbent polymer
  • the pulp and polymer absorb and retain moisture.
  • CaCl 2 calcium chloride
  • CaCl 2 calcium chloride
  • the polymer reacted with CaCl 2 as a decomposing agent is again in an irreversible state where it cannot absorb and retain moisture.
  • the third waste disposal apparatus 5 includes an input unit 10 having an input port for inputting used paper diapers, sanitary products, and sand for pets (hereinafter, also referred to as waste D).
  • waste D used paper diapers, sanitary products, and sand for pets
  • Part 20 chute 21, mixer 70, discharge path 11, first opening / closing valve 12, dilution tank 30, decomposing agent introducing device 13, deodorizing device 80, discharging section 14, drainage path 15, second opening / closing valve 16, separation section 40 , A first ventilation path 17, a negative pressure eliminating section 17A, a second ventilation path 18, and a third ventilation path 19.
  • Each of the charging unit 10, the crushing unit 20, the chute 21, the mixer 70, the dilution tank 30, the separating unit 40, and the trap 15A separates the waste D having a polymer capable of absorbing and holding moisture, and is connected in series. There are a plurality of processing units.
  • the processing amount that the downstream processing unit can process in one process is equal to or larger than the processing amount that the upstream processing unit can process in one process.
  • the processing amount that can be processed by the crushing unit 20 in one process is equal to or larger than the processing amount that can be processed by the input unit 10 in one process.
  • the processing amount that can be processed by the chute 21 in one processing is equal to or larger than the processing amount that can be processed by the crushing unit 20 in one processing.
  • the processing amount that can be processed by the mixer 70 in one process is equal to or larger than the processing amount that the chute 21 can process in one process.
  • the processing amount that the dilution tank 30 can process in one process is equal to or larger than the processing amount that the mixer 70 can process in one process.
  • the processing amount that can be processed by the separation unit 40 in one process is equal to or larger than the processing amount that the dilution tank 30 can process in one process.
  • the waste disposal apparatus 5 includes a first group G1, a second group G2, and a third group G3 each including a plurality of processing units.
  • the first group G ⁇ b> 1 includes a charging unit 10, a crushing unit 20, a chute 21, and a mixer 70.
  • the second group G2 includes a dilution tank 30.
  • the third group G3 includes the separation unit 40 and the trap 15A.
  • the waste disposal apparatus 5 forms a plurality of groups by one and / or a plurality of at least one treatment unit.
  • the charging section 10 extends in the up-down direction, has a cylindrical shape, and is opened at an upper end to form a charging port.
  • the input port is provided with a first lid 60 for opening and closing the input port.
  • a predetermined amount of filth D having a polymer capable of absorbing and retaining moisture is charged into the charging section 10.
  • the predetermined amount of filth D passes through the input unit 10 for about 5 seconds and is input into the crushing unit 20 described later.
  • the predetermined amount of the waste D is an amount that can be processed in the input unit 10 in one process.
  • the crushing unit 20 uses a crusher (for example, a known disposer or shredder).
  • the upper end of the crushing section 20 is connected to the lower end of the charging section 10.
  • a motor 20G for driving the crushing unit 20 is detachably attached to the side surface of the crushing unit 20 with respect to the crushing unit 20.
  • the operation of the motor 20G is controlled by a control unit (not shown).
  • the crushing unit 20 crushes a predetermined amount of the filth D charged into the input unit 10 in about 20 seconds to form a crushed material C including a predetermined amount of the filth D (hereinafter, also referred to as a crushed material C).
  • the control unit is configured as a control circuit including a microcomputer, for example, and has a CPU, a storage unit, and the like.
  • An operation unit (not shown) is electrically connected to the control unit, and the user of the waste disposal apparatus 5 operates the operation unit to start or end the operation of the waste disposal apparatus 5. It has a configuration that can be used.
  • a control unit is electrically connected to the motor 20G of the crushing unit 20.
  • the control unit is configured to detect the amount of power consumption consumed by the motor 20G of the crushing unit 20 and detect the first load related to the crushing unit 20 based on the detected amount of power consumption.
  • the chute 21 has a cylindrical shape formed by reducing the diameter from the upper end to the lower end, and the upper end is connected to the lower end of the crushing unit 20.
  • the chute 21 guides the crushed material C from the crushing unit 20 to a mixer 70 described later.
  • the crushed material C passes through the chute 21 for about 5 seconds and is charged into the mixer 70.
  • a second lid 22 is provided at a lower end of the chute 21.
  • the second lid 22 closes the lower end of the chute 21 when the crushed material C or the like is not placed.
  • the second lid 22 hangs down by the weight of the crushed material C or the like and releases the lower end of the chute 21.
  • the second lid 22 closes the lower end of the chute 21 again when the placed crushed material C or the like flows into the mixer 70.
  • the second lid 22 can prevent the later-described agitated material S from being scattered from the mixer 70 toward the crushing unit 20 and the charging unit 10 and prevent the odor from rising and rising.
  • the mixer 70 has its upper end connected to the lower end of the chute 21. On the lower surface of the mixer 70, a motor 70A for driving the mixer 70 is detachably attached to the mixer 70.
  • the mixer 70 agitates the crushed material C and the decomposing agent for about 60 seconds to form a stirred material S (hereinafter, also referred to as a stirred material S) containing a predetermined amount of filth D.
  • the control unit is electrically connected to the motor 70A of the mixer 70.
  • the control unit is configured to detect the magnitude of the current consumed by the motor 70A of the mixer 70 and to detect the second load related to the mixer 70 based on the detected magnitude of the consumed current.
  • the control unit determines whether there is only the agitated material S in the first group G1 (the charging unit 10, the crushing unit 20, the chute 21, and the mixer 70), and whether the first group G1 is empty. Is determined.
  • the first on-off valve 12 is, for example, a known electric ball valve.
  • the first on-off valve 12 is provided in the discharge path 11 and opens and closes the discharge path 11. The operation of opening and closing the first on-off valve 12 is controlled by the control unit.
  • a first manual opening / closing valve 12 ⁇ / b> A that is manually opened / closed is provided in the discharge path 11 on the upstream side of the first opening / closing valve 12.
  • the first manual on-off valve 12A is always open, and is closed when any one of the first group G1 and the second group G2 is removed from the waste disposal apparatus 5.
  • the discharge path 11 between the first manual open / close valve 12A and the first open / close valve 12 is configured so that the discharge path 11 can be freely separated into the first manual open / close valve 12A side and the first open / close valve 12 side.
  • a first connection portion 11A is provided.
  • first connection portion 11A for example, a flange portion is formed at the end of each of the discharge passages 11 on the first manual on-off valve 12A side and the first on-off valve 12 side, and the end surfaces of these flange portions are brought into contact with each other. I have.
  • the first connecting portion 11A is in communication with a holding member that holds the end surfaces of the flange portions in contact with each other (not shown).
  • the first connection portion 11A is provided with a first manual on-off valve 12A and a first on-off valve 12 in the vicinity, and connects the first group G1 and the second group G2.
  • the diluting tank 30 dilutes the agitated material S with at least one of water and hot water supplied from a discharge unit 14 described later and dilutes T containing a predetermined amount of filth D in about 85 seconds (hereinafter, diluent T Also called).
  • the other end of the discharge path 11 is connected to the upper surface of the dilution tank 30, and the discharge path 11 communicates with the inside of the dilution tank 30.
  • the dilution tank 30 communicates with the downstream side of the crushing section 20.
  • a motor 30A is detachably attached to the dilution tank 30.
  • a propeller (not shown) is detachably connected to the rotation shaft of the motor 30A in the dilution tank 30.
  • the propeller does not change its posture in the dilution tank 30 even when the motor 30A is removed.
  • the motor 30A is detachable from the dilution tank 30 and the propeller.
  • the operation of the motor 30A of the dilution tank 30 is controlled by the control unit.
  • the control unit is configured to be able to determine whether or not the second group G2 (dilution tank 30) is empty.
  • An inspection port 30B is formed on the side surface of the dilution tank 30.
  • the inspection port 30B is closed in a watertight manner by a lid 30C.
  • the lid 30C is removed, and the inside of the dilution tank 30 is inspected from the inspection port 30B.
  • the control unit is configured to be able to determine whether the inspection port 30B is closed or not closed by the lid 30C. When the control unit determines that the inspection port 30B is not closed by the lid 30C, the control unit controls the waste disposal apparatus 5 not to operate.
  • a control unit is electrically connected to the motor 30A of the dilution tank 30.
  • the control unit is configured to detect the magnitude of the current consumed by the motor 30A of the dilution tank 30, and to detect the third load related to the dilution tank 30 based on the detected magnitude of the consumed current. Specifically, it is assumed that when the magnitude of the current consumed by the motor 30A of the dilution tank 30 exceeds a predetermined value, the reaction of the polymer described later has not been completed.
  • the decomposing agent input device 13 inputs the decomposing agent into the chute 21.
  • the decomposing agent introducing device 13 is attached to a side surface of the chute 21.
  • a known feeder or the like is used as the decomposing agent introducing device 13, and the control unit controls the chute 21 to supply a predetermined amount of the decomposing agent.
  • the amount of the predetermined amount of the decomposing agent is an amount capable of uniformly extracting water from the polymer contained in the predetermined amount of the waste D.
  • the control unit of the decomposing agent charging device 13 is electrically connected.
  • the control unit supplies the decomposing agent from the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, the signal corresponding to the magnitude of the second load, and the signal corresponding to the magnitude of the third load.
  • the decomposing agent feeding device 13 is controlled so as to perform the above.
  • the deodorizing device 80 has an intake unit 80A, a deodorizing unit 80B, and a blowing unit 80C.
  • a known axial fan or the like is used for the intake section 80A.
  • the suction section 80A sucks in air from one end face and blows air from the other end face.
  • the suction unit 80A is electrically connected to the control unit.
  • the suction unit 80A is attached so as to cover the first connection port 10D formed on the side surface of the insertion unit 10 with one end surface.
  • the intake section 80A takes in air from the input section 10.
  • a so-called deodorizing filter formed of a nonwoven fabric or the like to which activated carbon is attached is used for the deodorizing section 80B.
  • the deodorizing section 80B is arranged so as to cover the other end face (that is, the air blowing face) of the suction section 80A.
  • the blower unit 80C has the same configuration as the suction unit 80A, and for example, a known axial fan or the like is used.
  • the blowing unit 80C is electrically connected to the control unit.
  • the blowing unit 80C is attached so as to cover the second connection port 10E formed on the side surface of the charging unit 10 with the other end surface.
  • the charging section 10 is open to the atmosphere via a deodorizing device 80.
  • the blowing unit 80C blows air to the charging unit 10.
  • the deodorizing device 80 deodorizes the odor generated from at least one of the waste D and the crushed material C.
  • the deodorizing device 80 is connected to the first connection port 10D and the second connection port 10E.
  • the discharge unit 14 supplies at least one of water and hot water to the crushing unit 20.
  • the discharge unit 14 has a first discharge unit 14A that supplies water and a second discharge unit 14B that supplies hot water.
  • the discharge unit 14 is provided in the input unit 10.
  • a first solenoid valve 14C and a second solenoid valve 14D are provided in each of the first ejection section 14A and the second ejection section 14B.
  • the first solenoid valve 14C and the second solenoid valve 14D are controlled by the control unit to supply water or hot water to the crushing unit 20 based on predetermined conditions. Specifically, the control unit counts the elapsed time since the driving of the motor 20G of the crushing unit 20 is stopped, counts the number of times the motor 20G of the crushing unit 20 is driven, and inputs the disintegrant. It is configured to be able to count the amount of the disintegration agent or the number of times the disintegrant has been charged or to count a predetermined time.
  • control unit determines at least one of a predetermined elapsed time after the operation of the crushing unit 20 has stopped, a predetermined number of times the crushing unit 20 has operated, a predetermined amount of the disintegrant, and a predetermined number of times of the injection.
  • discharge unit 14 is controlled so as to supply at least one of water and hot water at any one of the predetermined times. Thereby, the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 can be washed.
  • the drainage channel 15 is connected at one end to the lower end of the dilution tank 30. The other end of the drain 15 communicates with a sewer pipe (not shown).
  • a trap 15 ⁇ / b> A is formed in the drainage channel 15.
  • a jet drain section is connected to the trap 15A (not shown).
  • the drain 15 allows the water of the diluent T to flow toward the drain in about 5 seconds.
  • the second on-off valve 16 is, for example, a known electric ball valve.
  • the second on-off valve 16 is provided upstream of the trap 15 ⁇ / b> A of the drainage channel 15 and opens and closes the drainage channel 15. The operation of opening and closing the second on-off valve 16 is controlled by the control unit.
  • a second manual opening / closing valve 16 ⁇ / b> A that is manually opened / closed is provided in the drainage channel 15 on the upstream side of the second opening / closing valve 16.
  • the second manual on-off valve 16A is always open, and is closed when one of the second group G2 and the third group G3 is removed from the waste disposal apparatus 5.
  • the drainage channel 15 between the second manual on-off valve 16A and the second on-off valve 16 is configured so that the drainage channel 15 can be freely separated into the second manual on-off valve 16A side and the second on-off valve 16 side.
  • a second connection portion 15B is provided.
  • a flange portion is formed at an end of each of the drainage channels 15 on the second manual on-off valve 16A side and the second on-off valve 16 side, and end surfaces of these flange portions are brought into contact with each other. I have.
  • the second connection portion 15B is in communication with a holding member that holds the end surfaces of the flange portions in contact with each other (not shown).
  • the second connection portion 15B is provided with a second manual on-off valve 16A and a second on-off valve 16 in the vicinity, and connects the second group G2 and the third group G3.
  • the separation unit 40 is provided in the drainage channel 15 between the trap 15A and the second on-off valve 16.
  • the separation section 40 is connected to the downstream side of the dilution tank 30.
  • As the separation unit 40 for example, a known screw press device or the like is used.
  • a motor 40C for driving the separating unit 40 is detachably attached to the side of the separating unit 40 with respect to the separating unit 40.
  • a solids discharge section 40D for discharging solids separated from the diluent T is connected to the upper end of the separation section 40.
  • the separation unit 40 can separate and extract solids from the diluent T flowing through the drainage channel 15 in about 75 seconds.
  • the operation of the motor 40C of the separation unit 40 is controlled by the control unit.
  • the control unit is configured to be able to determine whether or not the third group G3 (separation unit 40) is empty.
  • An inspection port 40A is formed on the side surface of the separation unit 40.
  • the inspection port 40A is closed in a watertight manner by a lid 40B.
  • the lid 40B is removed, and the inside of the separation unit 40 is inspected from the inspection port 40A.
  • the control unit determines that the inspection port 40A is not closed by the lid 40B, the control unit controls the waste disposal apparatus 5 not to operate.
  • One end of the first ventilation path 17 communicates with the charging section 10 downstream of the first connection port 10D and the second connection port 10E, and the other end is connected to the upper end of the dilution tank 30 and communicates with the dilution tank 30. doing.
  • One end of the first ventilation path 17 is detachable from the charging section 10, and the other end is detachable from the dilution tank 30.
  • the negative pressure eliminating section 17A is attached to the first ventilation path 17.
  • a well-known Dolgo ventilation valve, a covert ventilation valve, or the like is used for example.
  • One end of the second ventilation path 18 is connected to and connected to the downstream side of the negative pressure eliminating section 17A of the first ventilation path 17, and the other end is connected to and connected to the upper end of the separation section 40. Communicating. The other end of the second ventilation path 18 is detachable from the separation section 40.
  • the negative pressure eliminating section 17A eliminates the negative pressure in the dilution tank 30 and the separation section 40 via the first ventilation path 17 and the second ventilation path 18.
  • the third ventilation path 19 has one end connected to and connected to the side surface of the charging section 10, and the other end connected to and connected to the solids discharge section 40 ⁇ / b> D of the separation section 40.
  • One end of the third ventilation path 19 is detachable from the charging section 10 and the other end is detachable from the solids discharge section 40D.
  • An intake unit 19A is attached to the third ventilation path 19.
  • the suction unit 19A has the same configuration as the blowing unit 80C and the suction unit 80A of the deodorizing device 80, and for example, a known axial fan or the like is used.
  • the suction unit 19A is electrically connected to the control unit.
  • the suction section 19A is attached to the third ventilation path 19 so that when the suction section 19A is driven, the air in the third ventilation path 19 flows from the solids discharge section 40D toward the charging section 10.
  • the processing times of the first group G1, the second group G2, and the third group G3 are substantially equal. Specifically, the processing time of each of the first group G1, the second group G2, and the third group G3 becomes shorter as the group is located on the downstream side. That is, the processing time of the group on the downstream side is shorter than that of the group on the upstream side.
  • each of the first group G1, the second group G2, and the third group G3 is configured to be removable from the waste disposal apparatus 5.
  • the motor 20G and the motor 70A are left inside the waste disposal apparatus 5.
  • the motor 30A is left inside the waste disposal apparatus 5.
  • the motor 40C is left inside the waste disposal apparatus 5.
  • the first ventilation path 17, the second ventilation path 18, and the third ventilation path 19 are left in the waste disposal apparatus 5 when any of the groups is removed.
  • the operation of the third waste disposal apparatus 5 will be described.
  • the first lid 60 is placed in an upright state, the inlet is opened, and a predetermined amount of waste D is injected into the inlet 10.
  • the control unit starts the operation of the suction unit 80A and the blower unit 80C of the deodorization device 80.
  • the first lid 60 is placed in the lying state, the slot of the slot 10 is closed, and the operation unit (not shown) is operated to operate the waste disposal apparatus 5.
  • the waste treatment device 5 first operates at least one of the first solenoid valve 14C and the second solenoid valve 14D by the control unit to remove at least one of the first predetermined amount of water and hot water from the discharge unit 14. It is supplied to the crushing unit 20. In this way, a predetermined amount of filth D and at least one of water and hot water are introduced into the crushing unit 20. At this time, the first manual on-off valve 12A is open and the first on-off valve 12 is closed.
  • the motor 20G of the crushing unit 20 has a state in which the first lid 60 has opened the charging port, a state in which the dissolving agent has not been charged, a state in which the inspection port 30B is not closed by the lid 30C, and a state in which the inspection port 40A is closed by the lid 40B.
  • the control unit determines that the state is not closed, the control unit controls so as not to drive.
  • Control is performed when the first lid 60 is closed, the dissolving agent is charged, the inspection port 30B is closed by the lid 30C, and the inspection port 40A is closed by the lid 40B.
  • the motor 20G of the crushing unit 20 is driven, and a predetermined amount of the waste D is crushed.
  • the control unit estimates the amount of the predetermined amount of filth D input based on the magnitude of the first load of the motor 20G. Specifically, the control unit detects the first load (that is, the power consumption of the motor 20G) related to the crushing unit 20 and crushes the waste D when the first load exceeds a predetermined value. Then, the amount of the waste D is estimated based on the time when the first load exceeds the predetermined value. A predetermined amount of filth D is crushed in the crushing unit 20 to become crushed material C. The control unit operates the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, and injects a predetermined amount of the decomposing agent into the chute 21. A predetermined amount of the decomposing agent supplied to the chute 21 flows into the mixer 70.
  • the first load that is, the power consumption of the motor 20G
  • the crushed material C, at least one of the first predetermined amount of water and hot water, and the predetermined amount of the decomposer are stirred, and the polymer having absorbed and retained the water is reacted with the decomposer.
  • the crushed material C, at least one of water and hot water, and a predetermined amount of the decomposing agent are stirred to form the stirred material S.
  • the controller detects the second load related to the motor 70A of the mixer 70. Specifically, the magnitude of the second load detected at this time is the magnitude of the current consumption of the motor 70A.
  • the control unit determines that the magnitude of the second load of the motor 70A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the agitated product S and the decomposing agent has not sufficiently proceeded)
  • the control unit decomposes.
  • the disintegrating agent injecting device 13 is controlled so that an agent is additionally injected from the injecting agent injecting device 13.
  • the motor 70A is continuously driven, and the mixer 70 can further promote the reaction between the polymer of the agitated substance S and the decomposing agent.
  • the crushed material C, at least one of the first predetermined amount of water and hot water, and the decomposing agent are agitated, and the crushed material C is converted into the agitated material S.
  • the reaction with can be further advanced.
  • the magnitude of the current consumption of the motor 70A (that is, the magnitude of the second load) is equal to or less than a predetermined value, the first group G1 is not empty, only the agitated material S exists, and the second group G2
  • the control unit determines that the inside is empty, the first open / close valve 12 in the closed state is opened by the control unit. Then, the agitated material S flows into the dilution tank 30 via the discharge path 11.
  • the first electromagnetic valve 14C and the second electromagnetic valve 14D of the discharge unit 14 are operated by the control unit to supply at least one of the second predetermined amount of water and hot water from the discharge unit 14 to the crushing unit 20.
  • At least one of the second predetermined amount of water and hot water is a predetermined amount with respect to the amount of the stirring object S.
  • the motor 20G of the crushing unit 20 and the motor 70A of the mixer 70 are being driven.
  • the inside of the crushing unit 20 and the inside of the mixer 70 can be washed while the stirred material S in the mixer 70 is surely conveyed into the dilution tank 30.
  • the first ventilation path 17 suppresses the inside of the dilution tank 30 from becoming a positive pressure when at least one of the crushed material C and the second predetermined amount of water and hot water flows into the dilution tank 30.
  • the second on-off valve 16 is in a closed state when at least one of the second predetermined amount of water and hot water and the agitated material S flow into the dilution tank 30, and the second manual on-off valve 16A is in an open state. It is.
  • a predetermined amount of the filth D is made into the stirrer S in about 90 seconds, and the stirrer S and at least one of the second predetermined amount of water and hot water flow into the second group G2.
  • the control unit detects that the inside of the first group G1 has changed from a non-empty state to an empty state, the control unit sets the open first on-off valve 12 to a closed state.
  • the first group G1 is again in a state in which a predetermined amount of the waste D can be made into the agitated material S. That is, the waste disposal apparatus 5 can perform the separation processing of the waste such as the waste D and the stirrer S in parallel in the first group G1 and the second group G2. Thereby, the waste disposal apparatus 5 can increase the throughput of the waste D as a whole.
  • the second predetermined amount of water and hot water and the stirred material S are diluted in the dilution tank 30 to make the stirred material S a diluted material T.
  • the second manual on-off valve 16A is open and the second on-off valve 16 is closed.
  • the drive of the motor 30A of the dilution tank 30 is started by the control unit.
  • the propeller (not shown) of the dilution tank 30 rotates, and the second predetermined amount of at least one of water and hot water and the agitated material S are agitated. Become.
  • the concentration of Ca (calcium) or Cl (chlorine) of the decomposing agent contained in the agitated material S in the agitated material S can be reduced by using the diluent T, and the Ca component adheres to the sewer pipe. It is possible to suppress that the sewer pipe is corroded due to hardening or Cl.
  • the third load on the motor 30A of the dilution tank 30 is monitored by the control unit. Specifically, the magnitude of the third load detected at this time is the magnitude of the current consumption of the motor 30A of the dilution tank 30.
  • control unit determines that the magnitude of the third load of the motor 30A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the diluent T and the decomposer has not sufficiently proceeded)
  • the decomposing agent input device 13 is controlled so that the decomposing agent is additionally input from the decomposing agent input device 13.
  • the motor 30A of the dilution tank 30 is also continuously driven, and the reaction between the polymer of the diluent T and the decomposing agent can be further advanced in the dilution tank 30.
  • the agitated material S and at least one of the second predetermined amount of water and hot water are agitated, and the agitated material S is diluted to the diluted material T in which the reaction between the polymer and the decomposing agent has progressed.
  • a configuration may be adopted in which a decomposing agent inlet is formed in the dilution tank 30 and a decomposing agent can be supplied from the decomposing agent input device 13 also to this decomposing agent inlet.
  • the decomposing agent can be directly injected into the dilution tank 30.
  • the solid content is separated from the diluent T.
  • the control unit determines that the magnitude of the current consumption of the motor 30A (that is, the magnitude of the third load) is equal to or smaller than a predetermined value, and that the second group G2 is not empty and the third group G3 is empty.
  • the control unit determines that the second open / close valve 16 is in the closed state
  • the second open / close valve 16 in the closed state is opened by the control unit.
  • the diluent T flows from the dilution tank 30 toward the separation unit 40.
  • the mixture S is turned into the diluent T in about 85 seconds, and the diluent T flows into the third group G3.
  • the control unit closes the open second on-off valve 16. In this way, the second group G2 is in a state where the stirred substance S can be turned into the diluted substance T again.
  • the waste disposal apparatus 5 can perform the separation processing of the waste such as the waste D, the agitated material S, and the diluent T in parallel in the first group G1, the second group G2, and the third group G3. Thereby, the waste disposal apparatus 5 can increase the throughput of the waste D as a whole.
  • the input port of the waste disposal apparatus 5 is closed by the first lid 60. For this reason, by taking in air from the negative pressure eliminating portion 17A of the first ventilation path 17 into the first ventilation path 17, it is possible to prevent the inside of the dilution tank 30 from becoming a negative pressure. , And can be satisfactorily flowed toward the separation section 40.
  • the drive of the motor 40C of the separation unit 40 is started by the control unit. At this time, the operation of the suction unit 19A is also started by the control unit.
  • the diluent T that has flowed into the drainage channel 15 flows into the separation unit 40, and the solid content of the diluent T is discharged from the solid discharge unit 40D by driving the motor 40C.
  • the solids of the diluent T discharged from the solids discharge unit 40D are taken into the collection bag 40E attached to the tip of the solids discharge unit 40D.
  • the odor generated in the solids discharge section 40D is guided to the input section 10 by the third ventilation path 19 and the suction section 19A.
  • the water of the diluent T flows through the trap 15A to a drain (not shown).
  • the separating section 40 is in communication with the first ventilation path 17 via the second ventilation path 18. Thereby, the inside of the separation unit 40 is suppressed from being negative pressure, and the water of the diluent T can be satisfactorily flowed from the separation unit 40 toward the sewer pipe.
  • the water of the diluent T remaining in the trap 15A is surely conveyed to the sewer pipe by vigorously supplying water to the trap 15A from a jet drain (not shown) connected to the trap 15A.
  • the third group G3 the solids can be separated from the diluent T in about 80 seconds, and the water of the diluent T can be flown to the sewer.
  • the inside of the third group G3 changes from a state that is not empty to an empty state, the third group G3 is in a state where the solids can be separated from the diluent T again.
  • the processing time of the third group G3 is shorter than the processing time of the first group G1 and the second group G2, and the processing time of the second group G2 is shorter than the processing time of the first group G1. For this reason, when the wastes such as the wastes D, the agitated materials S, and the diluents T are separated in parallel in each group, the processing in the downstream group ends earlier than the processing in the upstream group. Immediately after the processing is completed in the group, the stirred substance S and the diluted substance T can flow into the downstream group.
  • the motors 20G, 70A, 30A of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are operated. , 40C are stopped.
  • the control unit controls so that hot water is supplied from the second discharge unit 14B of the discharge unit 14.
  • the motors 20G, 70A, 30A, and 40C of the crushing unit 20 the mixer 70, the dilution tank 30, and the separation unit 40 are driven by the control unit, and the first on-off valve 12 and the second on-off valve 16 are opened.
  • the waste disposal apparatus 5 is cleaned so that the waste D, the crushed substance C, the agitated substance S, the diluent T, and the like do not remain in the waste disposal apparatus 5, and the Ca component is contained in the waste disposal apparatus 5. It is possible to suppress adhesion and solidification, and corrosion of the inside of the waste disposal apparatus 5 by Cl.
  • the first manual on-off valve 12A and the first on-off valve 12 are closed.
  • the discharge path 11 is separated into the first manual opening / closing valve 12A side and the first opening / closing valve 12 side at the first connection portion 11A.
  • one end of the first ventilation path 17 and one end of the third ventilation path 19 are removed from the charging section 10.
  • the crushing unit 20 is removed with the motor 20G left in the waste disposal apparatus 5.
  • the mixer 70 is removed with the motor 70A left in the waste disposal apparatus 5.
  • the first manual on-off valve 12A, the first on-off valve 12, the second manual on-off valve 16A, and the second on-off valve 16 are closed.
  • the discharge passage 11 is separated into the first manual opening / closing valve 12A side and the first opening / closing valve 12 side.
  • the drain passage 15 is connected to the second manual opening / closing valve 16A side. Disconnect from the second on-off valve 16 side.
  • the other end of the first ventilation path 17 is removed from the dilution tank 30.
  • the dilution tank 30 is removed in a state where the motor 30A is left in the waste disposal apparatus 5.
  • the second manual on-off valve 16A and the second on-off valve 16 are closed.
  • the drainage channel 15 is separated into the second manual on-off valve 16A side and the second on-off valve 16 side.
  • the other end of the second ventilation path 18 is removed from the separation section 40, and the other end of the third ventilation path 19 is removed from the solid content discharge section 40D.
  • the separation unit 40 is removed with the motor 40C left in the waste disposal apparatus 5.
  • the first ventilation path 17, the second ventilation path 18, and the third ventilation path 19 are left in the waste disposal apparatus 5 when any of the groups is replaced.
  • the waste disposal apparatus 5 removes only the portion of the first group G1, the second group G2, and the third group G3 that directly touches the waste such as the waste D, the crushed material C, the agitated material S, and the diluent T. be able to.
  • the waste disposal apparatus 5 is detachable for each of a first group G1, a second group G2, and a third group G3.
  • the third waste disposal apparatus 5 is configured such that the processing amount that can be processed by one processing of the downstream processing unit is equal to or larger than the processing amount that can be processed by the upstream processing unit by one processing.
  • the filth such as the filth D, the crushed material C, the agitated material S, and the diluent T, which have been processed by the processing unit on the side, can immediately flow into the processing unit on the downstream side. For this reason, the waste disposal apparatus 5 does not need to provide an intermediate tank or the like between the processing units.
  • the third waste disposal apparatus 5 can be downsized.
  • the third sewage treatment apparatus 5 forms a first group G1, a second group G2, and a third group G3, each of which includes one and a plurality of at least one processing unit.
  • the processing times of the second group G2 and the third group G3 are shorter in the downstream group than in the upstream group. For this reason, the waste disposal apparatus 5 can operate the first group G1, the second group G2, and the third group G3 in parallel, whereby the waste disposal apparatus 5 can reduce the amount of waste D processed as a whole. Can be increased.
  • the first connection portion 11A connecting the first group G1, the second group G2, and the third group G3 is provided with the first on-off valve 12, and the second connection portion 15B is provided with the first on-off valve 12.
  • Two on-off valves 16 are provided.
  • the waste disposal apparatus 5 uses the first opening / closing valve 12 and the second opening / closing valve 16 to control the waste D, the agitated material S, and the diluent T in the first group G1, the second group G2, and the third group G3. Can be performed separately and simultaneously.
  • the third waste disposal apparatus 5 is detachable for each of the first group G1, the second group G2, and the third group G3. For this reason, the waste disposal apparatus 5 can easily perform maintenance such as replacement of parts.
  • the waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus is an apparatus for processing a used paper diaper Dd as an object to be treated.
  • the disposable diaper is made of pulp, plastic, superabsorbent polymer (SAP, superabsorbent polymer, hereinafter simply referred to as polymer), or the like. Used disposable diapers are converted into pulp or polymer, and the moisture of dirt such as urine is absorbed. The water-absorbing performance of the polymer that has absorbed water is suppressed by performing the treatment using the treating agent.
  • the treating agent is a chemical containing divalent metal ions such as calcium chloride (CaCl 2 ) and calcium acetate (Ca (CH 3 COO) 2 ), and by reacting these with a polymer. Water is separated from the polymer that has absorbed the water, and the polymer from which the water has been separated is again brought into an irreversible state in which the water cannot be absorbed. Even in the case where the used disposable diaper Dd contains a polymer that does not absorb moisture, the treatment with the treatment agent renders it impossible to absorb moisture.
  • divalent metal ions such as calcium chloride (CaCl 2 ) and calcium acetate (Ca (CH 3 COO) 2
  • the fourth and fifth filth disposal apparatuses 6 include an input unit 10, a processing unit 90, and a control unit 50, as shown in FIG.
  • the dispensing section 10 is charged with a disposable diaper Dd as a processing object having a water-absorbing polymer.
  • the processing unit 90 performs the processing of the paper diaper Dd using the processing agent.
  • the processing section 90 includes the crushing section 20, the mixer 70, the dilution tank 30, and the separation section 40.
  • the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are driven by motors 20G, 70A, 30A, and 40C as driving units, respectively.
  • the control unit 50 includes a determination unit 51 that determines the state of the paper diaper Dd input from the input unit 10, and determines the amount of the processing agent to be input based on the state of the paper diaper Dd determined by the determination unit 51.
  • the waste disposal apparatus 6 includes a treatment agent introduction unit 23, a measurement unit 52, a notification unit 53, a storage unit 54, and a transmission unit 55, as shown in FIGS.
  • the processing agent input section 23 inputs the processing agent into the processing section 90.
  • the measuring unit 52 measures the number of the disposable diapers Dd input from the input unit 10.
  • the notification unit 53 reports information on the operation status of the waste disposal apparatus 6.
  • the storage unit 54 stores information on the operation status of the waste disposal apparatus 6.
  • the transmitting unit 55 transmits information on the operation status of the waste disposal apparatus 6 to the outside.
  • the loading section 10 has a tubular shape extending in the vertical direction as shown in FIG.
  • the upper end of the input unit 10 is an input port into which a used paper diaper Dd is input.
  • a first lid 60 for opening and closing the charging port is provided at the upper end of the charging section 10.
  • the charging unit 10 is provided with a deodorizing device (not shown).
  • the charging section 10 is provided with a discharge section 14.
  • the discharge unit 14 supplies water used for each processing and cleaning by the waste disposal apparatus 6.
  • the discharge unit 14 is provided with a solenoid valve 14E.
  • the opening and closing operation of the solenoid valve 14E is controlled by the control unit 50.
  • the discharge section 14 can supply not only water but also hot water of about 40 ° C. to 90 ° C.
  • an adhesive is used for a general disposable diaper. By performing each treatment using hot water, the pressure-sensitive adhesive of the disposable diaper can be softened more and the adhesion to the device can be suppressed. By periodically cleaning the device using hot water, the solid content of the disposable diaper attached to the device can be removed by cleaning.
  • the processing agent input section 23 inputs the processing agent into the processing section 90.
  • the processing agent charging section 23 is provided on a chute 21 of a processing section 90 described later, and charges the processing agent into the chute 21.
  • a known quantitative feeder or the like is used for the treatment agent input section 23, for example, a known quantitative feeder or the like is used.
  • the processing agent input unit 23 is controlled by the control unit 50, and inputs the processing agent at the input amount determined by the control unit 50.
  • the processing agent input unit 23 is controlled by the control unit 50 so as to input an amount of the solid processing agent determined based on the state of the paper diaper Dd.
  • the processing agent input section 23 of the present embodiment has a first processing agent input section 23A and a second processing agent input section 23B.
  • the first processing agent input section 23A inputs a processing agent containing calcium acetate.
  • the second processing agent input section 23B inputs the processing agent containing calcium chloride.
  • the processing agent input unit 23 can input the processing agent including calcium acetate and the processing agent including calcium chloride at a desired ratio from the two processing agent input units 23A and 23B. It is configured.
  • the control unit 50 controls both the treatment agent containing calcium acetate and the treatment agent containing calcium chloride in a form in which calcium acetate has a predetermined ratio.
  • the control unit 50 removes the calcium acetate from the first processing agent input unit 23A. The control for inputting only the processing agent including the control agent is executed.
  • the processing unit 90 is arranged in the order of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 from the upstream side of the processing.
  • the crushing unit 20 arranged at the most upstream side is connected to the lower end of the input unit 10, and the paper diaper Dd input from the input unit 10 is introduced.
  • the crushing part 20 is formed so as to penetrate up and down, and a crushing rotary blade (not shown) is rotatably arranged inside.
  • the crushing unit 20 according to the present embodiment performs a process in which a rotary blade (not shown) is internally rotated by a motor 20G to crush pulp, plastic, polymer, and the like, which constitute a disposable diaper Dd, as crushed materials C. Do.
  • a known disposer or shredder may be used as the crushing unit 20 is not limited to the one having the rotary blade, but may be one having a reciprocating blade or one having a different type of blade such as a rotary blade and a reciprocating blade.
  • the drive of the motor 20G of the crushing unit 20 is controlled by the control unit 50.
  • the crushing unit 20 is provided with a first measuring unit 20H that measures the amount of current consumed by a motor 20G that rotates the rotary blade. Based on the magnitude of the current consumption measured by the first measuring unit 20H, the state of the processing in the crushing unit 20 is determined by the determining unit 51.
  • the first measurement unit 20H functions as an information acquisition unit that acquires the amount of power consumption of the motor 20G as information on the operation state of the crushing unit 20. Specifically, the magnitude of the current consumption measured by the first measuring unit 20H is compared with a predetermined value to determine whether or not the crushing unit 20 is processing the paper diaper Dd. The details will be described later in the operation description.
  • a chute 21 for guiding the generated crushed material C to the mixer 70 is connected to a lower end of the crushing unit 20. As described above, the chute 21 is provided with the treatment agent charging section 23.
  • the mixer 70 is formed with an open top, and has a mixing rotary blade (not shown) rotatably disposed therein.
  • the mixer 70 has an upper end connected to the lower end of the chute 21.
  • the mixer 70 performs a process of mixing the crushed material C introduced from the crushing unit 20 via the chute 21 and the processing agent supplied from the processing agent input unit 23 provided in the chute 21 to generate a mixture M. .
  • the mixer 70 of the present embodiment mixes the crushed material C and the processing agent by rotating the rotary blade inside (in the cylinder) by the motor 70A.
  • the mixer 70 is not limited to the one having the rotary blade, but may be one having a reciprocating blade or one having a different type of blade such as a rotary blade and a reciprocating blade.
  • the driving of the motor 70A of the mixer 70 is controlled by the control unit 50.
  • the mixer 70 is provided with a second measuring unit 70B that measures the amount of current consumed by the motor 70A that rotates the rotary blade. Based on the magnitude of the current consumption measured by the second measuring unit 70B, the state of the processing in the mixer 70 is determined by the determining unit 51.
  • the second measurement unit 70B functions as an information acquisition unit that acquires the amount of power consumption of the motor 70A as information on the operation state of the mixer 70. Specifically, the magnitude of the current consumption measured by the second measuring unit 70B is compared with two predetermined values to determine whether or not the mixer 70 is processing the crushed material C. The details will be described later in the operation description.
  • a discharge path 11 for discharging the generated mixture M to the dilution tank 30 is connected to a lower side surface of the mixer 70.
  • the discharge path 11 is provided with a first on-off valve 12 for opening and closing the discharge path 11.
  • the opening / closing operation of the first opening / closing valve 12 is controlled by the control unit 50.
  • the first on-off valve 12 includes, for example, a known electric ball valve and the like.
  • the first on-off valve 12 is provided at one end of the discharge path 11 near the mixer 70.
  • the dilution tank 30 is formed by rotatably arranging a propeller (not shown) in an internal space. The other end of the discharge path 11 is connected to the dilution tank 30.
  • the dilution tank 30 dilutes the mixture M discharged from the mixer 70 via the discharge path 11 with water to generate a diluent T.
  • the dilution tank 30 dilutes the mixture M while rotating a propeller (not shown) in the tank by a motor 30A.
  • the driving of the motor 30A is controlled by the control unit 50.
  • the dilution tank 30 is provided with a third measuring unit 30D that measures the amount of current consumed by the motor 30A that rotates the propeller.
  • the state of processing in the dilution tank 30 is determined by the determining unit 51.
  • the third measurement unit 30D functions as an information acquisition unit that acquires the amount of power consumption of the motor 30A as information on the operation state of the dilution tank 30.
  • the magnitude of the consumed current measured by the third measuring unit 30D is compared with two predetermined values to determine whether or not the dilution tank 30 is processing the mixture M. The details will be described later in the operation description.
  • the dilution tank 30 is connected to one end of a drainage channel 15 for discharging the generated diluent T to the separation unit 40.
  • the drainage channel 15 is provided with a second on-off valve 16 for opening and closing the drainage channel 15.
  • the opening and closing operation of the second on-off valve 16 is controlled by the control unit 50.
  • the second on-off valve 16 includes, for example, a known electric ball valve or the like, like the first on-off valve 12.
  • the second on-off valve 16 is provided at one end of the drainage channel 15 near the dilution tank 30.
  • the separation unit 40 separates the diluent T generated in the diluting tank 30 into a solid content Sc such as pulp, plastic, and polymer and water L.
  • the separation unit 40 is configured to include, for example, a known screw press device or the like.
  • the separation unit 40 separates the diluent T by rotating a screw (not shown) by a motor 40C.
  • the driving of the motor 40C is controlled by the control unit 50.
  • the separation unit 40 is provided with a fourth measurement unit 40F that measures the magnitude of current consumption of a motor 40C that rotates the screw. Based on the magnitude of the current consumption measured by the fourth measuring unit 40F, the state of the processing in the separating unit 40 is determined by the determining unit 51.
  • the fourth measurement unit 40F functions as an information acquisition unit that acquires the amount of power consumption of the motor 40C as information on the operation state of the separation unit 40. Specifically, the magnitude of the current consumption measured by the fourth measurement unit 40F is compared with a predetermined value, and it is determined whether or not the separation unit 40 is processing the dilution T. The details will be described later in the operation description.
  • the separation unit 40 is connected to a solids discharge unit 40D that discharges the separated solids Sc and a downstream drain 15C that discharges the separated water L.
  • a collection bag 40E is detachably attached to the end of the solid content discharge unit 40D to store the collected solid content Sc.
  • the downstream drain 15C is connected to an external sewer, and the separated water L is discharged as it is.
  • a trap 15A is provided in the downstream drainage channel 15C.
  • a spout portion (not shown) is provided in the downstream drainage channel 15C, and water is spouted from the spout portion in the drainage direction, thereby forcibly discharging the water L retained in the trap 15A. be able to.
  • the measuring unit 52 is provided at the input port of the input unit 10.
  • the measurement unit 52 is configured to include a photoelectric sensor.
  • the measuring unit 52 measures the number of the disposable diapers Dd supplied to the input unit 10.
  • the measuring unit 52 can measure the number of disposable diapers Dd while determining the size of the disposable diapers Dd based on the detection time of the passing diapers Dd by the photoelectric sensor, for example, the difference between the stool diapers and the urine diapers. It is configured as follows.
  • the measurement result by the measurement unit 52 is sent to the control unit 50. What is measured by the measuring unit may be not only the number and size of the objects to be processed, but also the weight of the objects to be processed.
  • the control unit 50 controls each unit of the apparatus. Specifically, in the present embodiment, the control unit 50 controls the respective units 23A and 23B of the processing agent input unit 23, the drive control of the motors 20G, 70A, 30A and 40C of the processing unit 90, the electromagnetic valve 14E, the first Open / close control of the on-off valve 12 and the second on-off valve 16 is performed. In the present embodiment, the control unit 50 causes the determination unit 51 to determine the state of the paper diaper Dd based on the measurement result of the measurement unit 52. The determination unit 51 also determines the state of the paper diaper Dd based on the measurement results of the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F.
  • the determination unit 51 determines the first measuring unit 20H, the second measuring unit 70B, the third measuring unit 30D, and the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 of the processing unit 90. Then, the state of the disposable diaper Dd is determined based on the current consumption values of the motors 20G, 70A, 30A, 40C measured by the measuring units of the fourth measuring unit 40F.
  • the control unit 50 functions as an information acquisition unit that acquires information on the operation state of the processing unit 90. Specifically, the control unit 50 acquires the load reduction time of each unit (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) of the processing unit 90 as information on the operation state of the processing unit.
  • the load reduction time of the processing unit 90 is a time until the current consumption of each of the motors 20G, 70A, 30A, and 40C, which has been increased after the processing is started, is reduced to a predetermined value or less in each unit of the processing unit 90. .
  • control unit 50 controls the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F based on the fluctuations in the current consumption of the motors 20G, 70A, 30A, and 40C. , The load reduction time as information on the operation state of the processing unit 90 is acquired.
  • the determination unit 51 determines each part of the processing unit 90 (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit). The status of the unit 40) is determined. For example, the determination unit 51 determines each motor 20G as a measurement result measured by the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F as information on the operation state of the processing unit 90. , 70A, 30A, and 40C, the status of each unit (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) of the processing unit 90 can be determined. In this case, the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F function as an information acquisition unit that acquires a power consumption value as information regarding the operation state of the processing unit 90. .
  • the notification unit 53 is a display that displays information about the operation status of the waste disposal apparatus 6 in characters or graphics.
  • the notification unit 53 is arranged, for example, outside the input port of the input unit 10, as shown in FIG.
  • Examples of the information on the operating status notified by the notifying unit 53 include the state of the disposable diaper Dd as an object to be processed and information related thereto (for example, the number of disposable diapers Dd measured by the measuring unit 52, the weight of the disposable diaper Dd), The operating state of each part (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) of the processing unit 90 and information related thereto (for example, the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, And the state of each unit (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) of the processing unit 90 (for example, the current processing step, the processing of the disposable diaper Dd).
  • the storage unit 54 stores data of information listed as information on the operation status notified by the notification unit 53 and the like.
  • the storage unit 54 is a storage medium capable of storing such information data and a control program for the apparatus.
  • the storage unit 54 measures the measurement result of the measurement unit 52, the amount of the treatment agent supplied from the treatment agent introduction unit 23, and the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F.
  • Various information acquired during the operation of the waste disposal apparatus 6 such as a measured value to be performed, a load reduction time acquired by the control unit 50 based on the measured values, and a determination result of the determination unit 51 are related to the operation status of the waste disposal apparatus 6. Store as information.
  • the transmitting unit 55 transmits data of information listed as information on the operating status notified by the notifying unit 53 and the like.
  • the transmission unit 55 includes, for example, a known communication device or the like.
  • the information transmitted from the transmitting unit 55 can be received by an external receiving unit such as a management device of a management center or a portable terminal.
  • the control unit 50 starts the operation of the crushing unit 20 and the mixer 70 and executes control to close the first on-off valve 12 of the discharge path 11.
  • the processing of the disposable diaper Dd is started.
  • the measuring unit 52 counts the number of the disposable diapers Dd. Furthermore, in the case of the present embodiment, the measuring unit 52, which is a photoelectric sensor, measures the detection time for each paper diaper Dd.
  • the control unit 50 estimates the size of the paper diaper Dd. Specifically, the control unit 50 estimates whether the diaper is a stool diaper or a urine diaper in accordance with the length of the detection time of the diaper Dd measured by the measurement unit 52. When one disposable diaper is used, weighting is performed according to the type of disposable diaper, for example, by using 0.5 urinal disposable diapers. The control unit 50 determines the state of the disposable diapers Dd based on the number of disposable diapers Dd, which is the measurement result measured by the measuring unit 52, and determines the amount of the treatment agent to be introduced. The control unit 50 causes the processing agent input unit 23 to input the determined input amount of the processing agent (processing agent input step).
  • the processing agent including calcium acetate and the processing agent including calcium chloride are supplied from each of the first processing agent input section 23A and the second processing agent input section 23B.
  • the control unit 50 executes opening / closing control of the electromagnetic valve 14E, and supplies water according to the amount of the disposable diaper Dd measured by the measuring unit 52 from the discharge unit 14.
  • control unit 50 In the processing agent supply step, when the control unit 50 detects that the amount of the processing agent that can be supplied from the processing agent supply unit 23 is insufficient with respect to the determined supply amount, the control unit 50 executes control to stop the operation of the processing unit 90. .
  • the control unit 50 detects the shortage of the remaining amount with respect to the amount of the processing agent according to the number of the disposable diapers Dd, the control unit 50 stops each unit of the processing unit 90 and stops the processing. I do.
  • the control unit 50 causes the notification unit 53 to notify the shortage of the remaining amount of the processing agent.
  • control unit 50 when the control unit 50 confirms replenishment of the processing agent into the processing agent input unit 23, or when it is confirmed that the processing agent is manually input from the input port of the input unit 10, the control unit 50 performs processing. If it can be confirmed that the state has become normally executable, the control of automatically restarting the operation of the processing unit 90 may be executed.
  • the disposable diaper Dd supplied from the input unit 10 falls into the crushing unit 20 and is crushed (crushing step).
  • the crushing unit 20 crushes the paper diaper Dd together with the water supplied from the discharge unit 14.
  • the control unit 50 measures the magnitude of the current consumption of the motor 20G as information on the operation state of the processing unit by the first measurement unit 20H.
  • the measured current consumption value is stored in the storage unit 54.
  • the control unit 50 continues to rotate the rotary blade by controlling the drive of the motor 20G until the amount of current consumption becomes equal to or less than a predetermined value.
  • the disposable diaper Dd is finely crushed to be crushed material C and gradually falls to the lower chute 21, so that as the crushing proceeds, the load on the motor 20G gradually decreases.
  • the control unit 50 monitors the change of the value measured by the first measurement unit 20H, and determines the state of the crushing unit 20 by the determination unit 51.
  • the determining unit 51 determines that the state of the crushing unit 20 is “no load (idle operation)”. When the magnitude of the current consumption of the motor 20G measured by the first measuring unit 20H is not smaller than or equal to the predetermined value, the determining unit 51 determines that the state of the crushing unit 20 is “crushing”. When the state of the crushing unit 20 becomes “no load” within a predetermined time from “under crushing”, the determination unit 51 determines that the state is “crushed”. In this case, the control unit 50 stops the operation of the crushing unit 20 and starts the operation of the mixer 70.
  • the control unit 50 measures the processing time in the crushing unit 20, and determines an additional amount of the processing agent to be added according to the measurement result. Specifically, the control unit 50 estimates the number of the disposable diapers Dd based on the time when the state of the crushing unit 20 is “under crushing”, and compares the estimated number with the number of the disposable diapers Dd measured by the measuring unit 52. I do. When the estimated number of disposable diapers Dd is larger than the measurement result of the measuring unit 52, the control unit 50 determines an additional amount of the processing agent according to the difference, and causes the processing agent input unit 23 to additionally input the amount. On the other hand, when the estimated number of the disposable diapers Dd is smaller than the measurement result of the measurement unit 52, the control unit 50 determines the additional amount to be 0. That is, in this case, the control unit 50 does not add the processing agent.
  • the crushed material C dropped from the crushing unit 20 via the chute 21 is mixed by the mixer 70 (mixing step).
  • the crushed material C, the water supplied from the discharge unit 14, and the processing agent input from the processing agent input unit 23 are mixed in the mixer 70.
  • the polymer that has absorbed the water and the treating agent react with each other to generate a mixture M in which the solid component of the disposable diaper Dd containing the polymer and the water irreversibly separated from the polymer are mixed.
  • the control unit 50 measures the magnitude of the current consumption of the motor 70A by the second measuring unit 70B as information on the operation state of the processing unit.
  • the measured current consumption value is stored in the storage unit 54.
  • the control unit 50 controls the drive of the motor 70A and keeps rotating the rotary blade (not shown) until the magnitude of the current consumption becomes equal to or smaller than the predetermined magnitude.
  • the control unit 50 monitors the change of the value measured by the second measurement unit 70B, and determines the state of the mixer 70 by the determination unit 51.
  • the current consumption of the motor 70A of the mixer 70 is maintained at the value A for a while after executing the mixing process, and thereafter gradually decreases from the value A to reach the value B. Is maintained.
  • the current consumption of the motor 70A of the mixer 70 indicates the value A.
  • the current consumption of the motor 70A gradually decreases from the value A as the reaction between the polymer and the treatment agent progresses.
  • the current consumption of the motor 70A of the mixer 70 shows a value B smaller than the value A.
  • the determining unit 51 determines that the state of the mixer 70 is “no load (idle operation)”. I do.
  • This first predetermined value is set as a value smaller than the value B in FIG.
  • the determining unit 51 determines that the state of the mixer 70 is in the process of causing the polymer to react with the treating agent. It is determined that "polymer processing is in progress”.
  • This second predetermined value is set as a value smaller than the value A and larger than the value B in FIG.
  • the determination unit 51 determines that the state of the mixer 70 is “polymer processed”. In this case, the control unit 50 closes the second on-off valve 16 of the drain passage 15 and opens the first on-off valve 12 of the discharge passage 11 to introduce the mixture M into the dilution tank 30. At this time, the control unit 50 also starts the operation of the dilution tank 30.
  • the mixture M discharged from the mixer 70 is introduced into the dilution tank 30 via the discharge path 11 and is diluted (dilution process).
  • the mixture M is diluted by stirring the mixture M and water in the dilution tank 30.
  • the mixture M is diluted such that the concentration of the treating agent component contained in the mixture M becomes a predetermined value or less (for example, the chlorine concentration is 300 ppm or less).
  • a dilution T in which the mixture M is diluted to a concentration that can be discharged to the sewage is generated.
  • the determination unit 51 determines the number of the paper diapers Dd measured by the measurement unit 52 and the number of the paper diapers Dd estimated by the control unit 50 based on at least one of the measurement results of the first measurement unit 20H.
  • the state of the paper diaper Dd as a processing object is determined, and the control unit 50 supplies a predetermined amount of water from the discharge unit 14 according to the determination result of the determination unit 51.
  • water is supplied to the dilution tank 30 while washing the crushing unit 20, the chute 21, the mixer 70, and the discharge path 11. Since calcium acetate as a treating agent does not contain Cl (chlorine), the amount of water to be diluted can be reduced as compared with the case where only calcium chloride is used as a treating agent as in the related art.
  • the control unit 50 measures the magnitude of the current consumption of the motor 30A by the third measurement unit 30D as information on the operation state of the processing unit.
  • the measured current consumption value is stored in the storage unit 54.
  • the control unit 50 controls the driving of the motor 30A and keeps rotating the propeller (not shown) until the amount of current consumption becomes equal to or smaller than a predetermined value.
  • the viscosity decreases as the water content of the mixture M increases, so that the load on the motor 30A gradually decreases.
  • the control unit 50 monitors the fluctuation of the value measured by the third measurement unit 30D, and determines the state of the dilution tank 30 by the determination unit 51.
  • the determining unit 51 determines that the state of the dilution tank 30 is “no load (idle operation)”. judge.
  • the determination unit 51 determines that the state of the dilution tank 30 is “dilution process”. This second predetermined value is set as a value larger than the first predetermined value.
  • the determination unit 51 determines that the state of the dilution tank 30 is “diluted”. In this case, the control unit 50 opens the second on-off valve 16 of the drainage channel 15 to discharge the diluent T from the dilution tank 30 and starts the operation of the separation unit 40.
  • the diluent T discharged from the dilution tank 30 is introduced into the separation unit 40 via the drainage channel 15 and is separated (separation step).
  • the diluent T is separated into the solid content Sc and the water L in the separation unit 40.
  • the solid content Sc separated in the separation unit 40 is stored in the collection bag 40E via the solid content discharge unit 40D.
  • the water L separated in the separation section 40 is discharged from the downstream drainage channel 15C, and discharged to the external sewer through the trap 15A.
  • the trap 15A there is a possibility that the solid content Sc discharged to the downstream drainage channel 15C without being separated in the separation unit 40 may stay. Eject periodically to force discharge.
  • the control unit 50 measures the magnitude of the current consumption of the motor 40C by the fourth measurement unit 40F as information on the operation state of the processing unit.
  • the measured current consumption value is stored in the storage unit 54.
  • the control unit 50 continues to rotate the screw by controlling the drive of the motor 40C until the amount of current consumption becomes equal to or less than a predetermined amount.
  • the load on the motor 40C gradually decreases as the separation of the solid content Sc and the water L from the diluent T progresses.
  • the control unit 50 monitors the change of the value measured by the fourth measurement unit 40F, and determines the state of the separation unit 40 by the determination unit 51.
  • the determining unit 51 determines that the state of the separating unit 40 is “no load (idle operation)”. When the magnitude of the current consumption of the motor 40C measured by the fourth measuring unit 40F is equal to or larger than a predetermined value, the determining unit 51 determines that the state of the separating unit 40 is “separating”. When the status of the separation unit 40 changes from “state of separation processing” to “no load” within a predetermined time, the determination unit 51 determines that the state of the separation unit 40 is “separation processing completed”. Is determined. In this case, the control unit 50 stops the operation of the separation unit 40. Thus, the processing of the disposable diaper Dd is completed.
  • the determination unit 51 determines that an abnormality has occurred. Specifically, it is conceivable that the paper diaper Dd may be jammed in the charging section 10 on the upstream side of the crushing section 20. In this case, the determination unit 51 determines that an abnormality of “clogging” has occurred in the crushing process. In this case, the control unit 50 stops the operation of the crushing unit 20 and causes the notification unit 53 to notify that an abnormality has occurred in the crushing process. In this case, the operator opens the first lid 60 and checks the inside of the input unit 10 to eliminate the jam of the paper diaper Dd. Thereafter, the operation of the crushing unit 20 is restarted.
  • the determination unit 51 determines that excessive input of the disposable diaper Dd or accumulation of dirt has occurred (“overload”). Is determined). In this case, the control unit 50 stops the operation of the crushing unit 20 and causes the notifying unit 53 to notify. In this case, the operator opens the first lid 60 and checks the amount of the disposable diaper Dd in the dispensing section 10. When it is confirmed that the disposable diapers Dd are excessively loaded, some disposable diapers Dd are taken out. On the other hand, when it is confirmed that the number of the disposable diapers Dd in the input unit 10 is equal to or less than the normal number, accumulation of dirt is assumed. In this case, the washing mode of the crushing unit 20 is executed. That is, the washing mode of the crushing unit 20 is started by an operator operating an operation button after an abnormal state is confirmed by the operator.
  • the control unit 50 When the washing mode of the crushing unit 20 is started by the operation of the operation button by the operator, the control unit 50 first stops the operation of the crushing unit 20 and performs the mixing process which is the next process of the crushing process. Upon completion, the mixer 70 is emptied. Next, the control unit 50 executes a control of repeating the forward rotation and the reverse rotation drive of the motor 20G while supplying water from the discharge unit 14. Thereafter, the control unit 50 controls the motor 20G until the crushing unit 20 enters the “no load” state, that is, until the current consumption of the motor 20G measured by the first measuring unit 20H becomes smaller than a predetermined value. Drive forward. While the crushing unit 20 is executing the cleaning mode, the control unit 50 notifies the notification unit 53 that the crushing unit 20 is executing the cleaning mode.
  • the washing mode of not only the crushing unit 20 but also each unit of the processing unit 90 described below is performed using hot water. This is because accumulated dirt is easier to remove than washing using only water.
  • the cleaning mode of the crushing unit 20 for example, calcium acetate as a treatment agent may be manually input from the input unit 10.
  • the calcium acetate may be a solid or an aqueous solution.
  • the determination unit 51 If an abnormality occurs in the mixing process, for example, if the state of “no load” does not change even after a predetermined time has elapsed even though the operation of the mixer 70 has been started, the determination unit 51 generates an abnormality. It is determined that it has been performed. Specifically, it is conceivable that clogging of the crushed material C has occurred in the chute 21 on the upstream side of the mixer 70. In this case, the determination unit 51 determines that an abnormality of “clogging” has occurred in the mixing process. In this case, the control unit 50 operates the crushing unit 20 while supplying water from the discharge unit 14, and causes the crushed material C stuck in the chute 21 to drop into the mixer 70.
  • control unit 50 confirms that the abnormal state of the mixer 70 has been resolved, the normal operation of the mixer 70 is restarted. On the other hand, if the abnormal state of the mixer 70 has not been eliminated, the control unit 50 causes the notification unit 53 to notify that an abnormality has occurred in the mixing process, and stops the entire waste disposal apparatus 6.
  • the determination unit 51 determines that the reaction between the polymer and the processing agent is not sufficient. In this case, the control unit 50 executes control to cause the processing agent input unit 23 to input an additional processing agent.
  • the input amount of the treatment agent is determined based on the measurement value of the second measurement unit 70B at the time when the reaction is determined to be insufficient. That is, the determination unit 51 determines the degree of progress of the process of causing the polymer in the state of the paper diaper Dd to react with the processing agent based on the value of the current consumption of the motor 70A measured by the second measurement unit 70B.
  • the control unit 50 determines the amount of the processing agent to be re-input from the processing agent input unit 23 based on this.
  • the determination unit 51 determines that accumulation of dirt has occurred (“cleaning required”). Is determined). In this case, the control unit 50 stops the operation of the mixer 70 and executes the cleaning mode of the mixer 70. In the cleaning mode of the mixer 70, the control unit 50 controls the motor 70A while supplying water from the discharge unit 14 and supplying the processing agent from the processing agent input unit 23 with the first on-off valve 12 of the discharge path 11 closed. The control for repeating the forward rotation and the reverse rotation drive is executed. The processing agent supplied in the cleaning mode is only the processing agent containing calcium acetate supplied from the first processing agent supply section 23A.
  • the control unit 50 controls the motor 70A until the mixer 70 enters the “polymer-processed” state, that is, until the magnitude of the current consumption of the motor 70A measured by the second measurement unit 70B becomes smaller than a predetermined value. Drive forward. While the cleaning mode of the mixer 70 is being executed, the control unit 50 notifies the notification unit 53 that the cleaning mode of the mixer 70 is being executed. When the control unit 50 confirms that the state of the mixer 70 has changed from the “polymer processing” state to the “polymer processed” state, the control unit 50 stops the notification by the notification unit 53. On the other hand, if the abnormal state of the mixer 70 is not resolved, the control unit 50 notifies the notification unit 53 of the fact and stops the entire waste disposal apparatus 6.
  • the determination unit 51 performs the dilution step. It is determined that an abnormality has occurred in. Specifically, it is conceivable that the mixture M may have clogged in the discharge path 11 on the upstream side of the dilution tank 30. In this case, the control unit 50 repeats the opening and closing of the first on-off valve 12 on the upstream side of the dilution tank 30 a predetermined number of times in a state where the second on-off valve 16 of the drainage channel 15 on the downstream side of the dilution tank 30 is closed.
  • control unit 50 confirms that the abnormal state of the dilution tank 30 has been resolved, the normal operation of the dilution tank 30 is restarted. On the other hand, if the abnormal state of the dilution tank 30 has not been eliminated, the control unit 50 causes the notification unit 53 to notify that the abnormality has occurred in the dilution process, and stops the entire waste disposal apparatus 6.
  • the control unit 50 determines that the dilution is not sufficient, and performs control to additionally supply water from the discharge unit 14. Execute.
  • the supply amount of the water to be additionally supplied is determined based on the measurement value of the third measurement unit 30D at the time when the dilution is determined to be insufficient. That is, the determination unit 51 determines the state of the dilution tank 30 (the degree of progress of the dilution process) based on the value of the current consumption of the motor 30A measured by the third measurement unit 30D.
  • the control unit 50 determines the supply amount of water to be resupplied from the discharge unit 14 based on this.
  • the determination unit 51 determines that accumulation of dirt has occurred in the dilution tank 30 ( It is determined that “cleaning is required”). In this case, the control unit 50 stops the operation of the dilution tank 30 and executes the cleaning mode of the dilution tank 30. In the washing mode of the dilution tank 30, the control unit 50 supplies water from the discharge unit 14 in a state where the first opening / closing valve 12 of the discharge passage 11 is open and a state where the second opening / closing valve 16 of the drain passage 15 is closed.
  • the control for repeating the forward rotation and the reverse rotation driving of the motor 70A of the mixer 70 and the motor 30A of the dilution tank 30, respectively, is executed.
  • the processing agent supplied in the cleaning mode is only the processing agent containing calcium acetate supplied from the first processing agent supply section 23A.
  • the control unit 50 keeps the state until the dilution tank 30 is in the “diluted” state, that is, the state in which the magnitude of the current consumption of the motor 30A measured by the third measuring unit 30D is not equal to or more than the second predetermined value.
  • the motor 70A and the motor 30A are driven until the operation is completed.
  • the control unit 50 While the cleaning mode of the dilution tank 30 is being executed, the control unit 50 notifies the notification unit 53 that the cleaning mode of the dilution tank 30 is being executed.
  • the control unit 50 confirms that the state of the dilution tank 30 is in the state of “diluted”, the control unit 50 stops the notification by the notification unit 53.
  • the control unit 50 notifies the notification unit 53 of the fact and stops the entire waste disposal apparatus 6.
  • the determination unit 51 determines that the abnormality is It is determined that an error has occurred. Specifically, it is conceivable that the diluent T may have clogged in the drainage channel 15 on the upstream side of the separation unit 40. In this case, the control unit 50 executes control to repeat opening and closing of the second on-off valve 16 a predetermined number of times while operating the separation unit 40. Meanwhile, the control unit 50 causes the notification unit 53 to notify that an abnormality has occurred in the separation process.
  • control unit 50 determines that the abnormal state of the separation unit 40 has been resolved.
  • the control unit 50 causes the notification unit 53 to notify that the abnormality has occurred in the separation process, and stops the entire waste disposal apparatus 6.
  • the determination unit 51 determines that accumulation of dirt in the separation unit 40 has not occurred. It is determined that the occurrence has occurred (determined as "needs cleaning"). In this case, the control unit 50 executes the cleaning mode of the separation unit 40. In the cleaning mode of the separation unit 40, the control unit 50 controls the supply of water from the discharge unit 14 and the input of the treatment agent with the first on-off valve 12 of the discharge path 11 and the second on-off valve 16 of the drainage path 15 opened.
  • control is performed to repeat the forward rotation and the reverse rotation of the motor 70 A of the mixer 70, the motor 30 A of the dilution tank 30, and the motor 40 C of the separation unit 40, respectively.
  • the processing agent supplied in the cleaning mode is only the processing agent containing calcium acetate supplied from the first processing agent supply section 23A.
  • the control unit 50 controls the motors 70A and 70A until the separation unit 40 is in the “no load” state, that is, until the magnitude of the current consumption of the motor 40C measured by the fourth measurement unit 40F is not a predetermined value or more.
  • the motor 30A and the motor 40C are each driven.
  • the control unit 50 causes the notification unit 53 to notify that the cleaning mode of the separation unit 40 is being executed.
  • the control unit 50 confirms that the state of the separation unit 40 has become “no load”
  • the control unit 50 stops the notification by the notification unit 53.
  • the control unit 50 notifies the notification unit 53 of the fact and stops the entire waste disposal apparatus 6.
  • the waste disposal apparatus 6 performs the second processing after a predetermined time has elapsed from the start of the processing in any of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40.
  • the control unit 50 performs processing based on the difference between the measurement values and the assumed values. At least one of the additional introduction of the agent and the additional supply of water is executed.
  • the control unit 50 executes a control to notify the operating unit 53 of the operation status while the waste disposal apparatus 6 is processing the paper diaper Dd.
  • the control unit 50 determines that the operation status of the processing unit 90 is normal if the processing by the processing unit 90 is normal in addition to the abnormality content at the time of occurrence of the abnormality as described above as the operation status of the waste disposal apparatus 6. , The current process, and the time to the end are notified to the notifying unit 53.
  • the control unit 50 causes the storage unit 54 to store information regarding various operating states of the waste disposal apparatus 6 as data, and causes the transmission unit 55 to transmit the information externally.
  • FIG. 9 shows the relationship between the number of times of processing (horizontal axis) and the load reduction time (vertical axis) of the motor 70A when processing the disposable diaper Dd as an object to be processed in the mixer 70 as each unit of the processing unit 90.
  • the load reduction time is a time from when the processing is started in each unit of the processing unit 90 until the current consumption value of the motor, which has risen once, decreases to a predetermined value.
  • the current consumption value of the motor 70A decreases as the reaction between the polymer and the processing agent progresses.
  • the current consumption value of the motor 70A decreases to a predetermined value or less within a predetermined time when a normal process is performed in the mixer 70.
  • the control unit 50 acquires the load reduction time as the information on the operation state based on the information on the operation state measured by the measurement unit, measures the load reduction time, and stores it in the storage unit 54.
  • the control unit 50 predicts the future state of the mixer 70 based on the past load reduction time stored in the storage unit 54 while storing the same. That is, the control unit 50 obtains the load reduction time based on the magnitude of the current consumption of the motor 70A measured by the second measuring unit 70B as an information obtaining unit that obtains information on the operation state of the processing unit.
  • the determination unit 51 determines the state of the processing in the mixer 70 based on the load reduction time as information on the operation state of the processing unit. Further, the determination unit 51 predicts the processing status of the mixer 70 based on the past load reduction time stored in the storage unit 54.
  • the control unit 50 acquires the load reduction time based on the current consumption value of the motor 70A measured by the second measurement unit 70B, and stores the load reduction time in the storage unit 54.
  • a regression analysis is performed by linear regression on the measured values of a plurality of recent times (for example, 10 times) of the past load reduction times, and the upper limit value is exceeded within several times (for example, 20 times). Predict whether or not.
  • the determination unit 51 determines that the situation requires the cleaning of the mixer 70.
  • the control unit 50 executes the cleaning mode of the mixer 70.
  • the control unit 50 causes the notification unit 53 to execute notification.
  • the prediction of the state of the processing unit 90 by the determination unit 51 can be similarly performed not only in the mixer 70 but also in the crushing unit 20, the dilution tank 30, and the separation unit 40.
  • the crushing unit 20 it is possible to determine whether the load reduction time acquired based on the current consumption value of the motor 20G measured by the first measuring unit 20H is within a predetermined range, and to determine the load acquired in the past. By performing a regression analysis on the numerical values for the latest plurality of times in the reduction time, it is possible to predict whether or not the upper limit value is exceeded within a predetermined number of times.
  • the dilution tank 30 it is possible to determine whether or not the load reduction time acquired based on the current consumption value of the motor 30A measured by the third measuring unit 30D is within a predetermined range, and to determine the load acquired in the past. By performing a regression analysis on the numerical values for the latest plurality of times in the reduction time, it is possible to predict whether or not the upper limit value is exceeded within a predetermined number of times.
  • the separation unit 40 it is possible to determine whether the load reduction time acquired based on the current consumption value of the motor 40C measured by the fourth measurement unit 40F is within a predetermined range, and to determine the load acquired in the past. By performing a regression analysis on the numerical values for the latest plurality of times in the reduction time, it is possible to predict whether or not the upper limit value is exceeded within a predetermined number of times.
  • the prediction of the state of the processing unit 90 by the determination unit 51 includes, as information on the operating state, the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 30D.
  • the prediction unit 50 By performing regression analysis by linear regression on the current consumption value measured by the measurement unit 40F and the measured values of the power consumption values of the latest multiple times (for example, 10 times), within several times (for example, 20 times) It is also possible to predict whether or not at least one of the upper limit value and the lower limit value will be exceeded.
  • the waste disposal apparatus 6 determines the state of the disposable diaper Dd as the processing object input from the input unit 10, and performs processing based on the determined state. Determine the dosage of the agent. Therefore, an appropriate amount of the treatment agent can be easily grasped.
  • the waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus can suppress the occurrence of trouble due to excess or deficiency of the treatment agent.
  • the waste disposal apparatus 6 has the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the control unit 50 as the information acquisition unit. And the current consumption values of the motors 20G, 70A, 30A, and 40C of the respective units (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) measured by the fourth measuring unit 40F. .
  • This consumed current value is stored in the storage unit 54.
  • the determination unit 51 determines the state of the processing unit 90 based on the current consumption value as information on the operating state of the processing unit 90 acquired by the control unit 50. As described above, since the state of the processing unit 90 is determined by the determination unit 51, it is possible to reduce the variation in the determination result as compared with the case where the operator determines.
  • the waste disposal apparatus 6 of the sixth embodiment of the fifth waste disposal apparatus can more accurately grasp the status of the processing unit 90.
  • the waste disposal apparatus 6 includes a treatment agent input section 23 that inputs a processing agent into the processing section 90 and a measurement section 52 that measures the number of disposable diapers Dd input from the input section 10. And The determination unit 51 determines the state of the paper diaper Dd based on the measurement result of the measurement unit 52.
  • the control unit 50 causes the processing agent input unit 23 to input the determined input amount of the processing agent. For this reason, the number of disposable diapers Dd can be measured by the measuring unit 52 immediately after the dispensing, so that the state can be quickly determined.
  • the control unit 50 causes the processing agent input unit 23 to input an appropriate amount of the processing agent based on the determination result. As a result, the processing agent can be promptly and appropriately charged to perform the processing.
  • the waste disposal apparatus 6 according to the sixth embodiment of the fourth waste disposal apparatus is provided with a notification unit 53 that reports information on the operation status of the waste disposal apparatus 6. Therefore, it is possible to assist the user in easily grasping the operation status of the waste disposal apparatus 6.
  • the waste disposal apparatus 6 according to the sixth embodiment of the fourth waste disposal apparatus includes a storage unit 54 for storing information on the operation status of the waste disposal apparatus 6. For this reason, the user can be easily notified of the past operation status.
  • the waste disposal apparatus 6 according to the sixth embodiment of the fourth waste disposal apparatus includes a transmission unit 55 that transmits the operating status of the waste disposal apparatus 6 to the outside. Therefore, the operation status of the waste disposal apparatus 6 can be grasped from outside.
  • the control unit 50 measures the processing time in the crushing unit 20, determines the additional amount of the processing agent according to the measurement result, and determines the amount.
  • the processing agent of the supplied amount is injected from the processing agent input unit 23. Therefore, appropriate processing can be reliably performed.
  • the waste disposal apparatus 6 is configured such that the control unit 50 as the information acquisition unit controls the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit.
  • the current consumption values of the motors 20G, 70A, 30A, and 40C of the respective units of the processing unit 90 (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) measured by 40F are acquired. This consumed current value is stored in the storage unit 54.
  • the determination unit 51 determines the state of the processing unit 90 based on the current consumption value as information on the operating state of the processing unit 90 acquired by the control unit 50. As described above, since the state of the processing unit 90 is determined by the determination unit 51, it is possible to reduce the variation in the determination result as compared with the case where the operator determines. As a result, the status of the processing unit 90 can be grasped more accurately.
  • the determination unit 51 predicts the state of the processing unit 90 based on the information on the past operation state stored in the storage unit 54. Therefore, it is possible to prevent the processing unit 90 from operating in an abnormal state.
  • the waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus when the situation of the processing unit 90 predicted by the determination unit 51 is a predetermined situation, that is, When it is predicted that the load reduction time of each unit (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) exceeds a predetermined value, a cleaning mode as a cleaning operation for cleaning each unit of the processing unit 90. Execute For this reason, occurrence of an abnormality in the processing unit 90 can be suppressed.
  • the waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus when the situation of the processing unit 90 predicted by the determination unit 51 is a predetermined situation, that is, If it is predicted that the current consumption of the motors 20G, 70A, 30A, and 40C of each part (the crushing part 20, the mixer 70, the dilution tank 30, and the separation part 40) exceeds a predetermined value, each part of the processing part 90 A cleaning mode as a cleaning operation for cleaning is performed. For this reason, occurrence of an abnormality in the processing unit 90 can be suppressed.
  • the determination unit 51 re-determines the status of the processing unit 90 after performing the cleaning mode. For this reason, it is possible to reliably grasp whether or not the abnormal state of the processing unit 90 has been resolved.
  • the waste disposal apparatus 6 according to the sixth embodiment of the fourth and fifth waste disposal apparatuses is provided with a transmission unit 55 that transmits information on the operating state to the outside. Therefore, the status of the processing unit 90 can be grasped from outside.
  • the transmission unit 55 transmits the information on the operation state of each processing unit transmitted from the transmission units of the plurality of filth disposal apparatuses.
  • the information about the operating state is transmitted to an external receiving unit that receives the information. Therefore, it is possible to transmit information on the operation state of the processing unit 90 to a management device or the like of a management center that manages the states of the processing units of the plurality of devices.
  • each of the mixer 70, the dilution tank 30, and the separation unit 40 as a processing unit is in an abnormal state by the control unit 50. It is automatically determined that there is, and a washing mode, which is an operation mode for eliminating them, is automatically started. For this reason, it is possible to reduce the labor involved in the maintenance of the waste disposal apparatus 6.
  • the waste disposal apparatus 6 of Embodiment 6 of the fourth and fifth waste disposal apparatuses uses calcium acetate as a treatment agent. For this reason, when the components of the adhesive such as hot melt are contained in the disposable diaper Dd to be processed, the acetic acid is used in a process in which the components of the adhesive accompanied by pressure or sliding by a rotary blade or the like are likely to adhere. Can suppress the adhesion of the pressure-sensitive adhesive. Even when the adhesive is adhered, the adhesive is easily peeled off and can be suitably removed.
  • the waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus is provided with a second treatment agent introduction part 23B for introducing a treatment agent containing calcium chloride for suppressing the water absorption performance of the polymer.
  • a second treatment agent introduction part 23B for introducing a treatment agent containing calcium chloride for suppressing the water absorption performance of the polymer.
  • the waste disposal apparatus 6 of Embodiment 6 of the fourth and fifth waste disposal apparatuses uses calcium acetate as a treatment agent. Therefore, the device can be kept in a sanitary state by the bactericidal action of acetic acid.
  • the determination unit 51 determines the status of the processing unit 90 based on the load reduction time stored in the storage unit 54 as the information on the past operation state. Predict. Therefore, it is possible to prevent the processing unit 90 from operating in an abnormal state.
  • the waste disposal apparatus 6 determines the state of the disposable diaper Dd as an object to be treated introduced from the introduction section 10 and, based on the determined state, from the treatment agent introduction section 23.
  • the amount of the processing agent to be charged is determined. Therefore, an appropriate amount of the treatment agent can be easily grasped. As a result, it is possible to suppress the occurrence of a problem due to excess or deficiency of the processing agent.
  • the waste disposal apparatus 6 includes a processing agent input section 23 for inputting a processing agent to the processing section 90 and a measuring section 52 for measuring the number of disposable diapers Dd input from the input section 10.
  • the determination unit 51 determines the state of the paper diaper Dd based on the measurement result of the measurement unit 52.
  • the control unit 50 causes the processing agent input unit 23 to input the determined input amount of the processing agent. For this reason, the number of disposable diapers Dd can be measured by the measuring unit 52 immediately after the dispensing, so that the state can be quickly determined.
  • the control unit 50 causes the processing agent input unit 23 to input an appropriate amount of the processing agent based on the determination result. As a result, the processing agent can be promptly and appropriately charged to perform the processing.
  • the waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus is provided with a notification unit 53 that reports information on the operation status of the waste disposal apparatus 6. Therefore, it is possible to assist the user in easily grasping the operation status of the waste disposal apparatus 6.
  • the storage unit 54 stores information on the operation status of the waste disposal apparatus 6. For this reason, the user can be easily notified of the past operation status.
  • the waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus includes a transmission unit 55 that transmits the operating status of the waste disposal apparatus 6 to the outside. Therefore, the operation status of the waste disposal apparatus 6 can be grasped from outside.
  • control unit 50 measures the processing time in the crushing unit 20, determines the additional input amount of the processing agent according to the measurement result, and determines the amount.
  • the processing agent of the supplied amount is injected from the processing agent input unit 23. Therefore, appropriate processing can be reliably performed.
  • the deodorizing apparatus has a blower.
  • a ventilation path communicating with the second connection port may be provided from the other end face of the intake section with a deodorizing section interposed.
  • a restricting portion is provided in the air passage to restrict air from flowing from the second connection port toward the intake port, and not to restrict air from flowing from the intake port to the second connection port.
  • An exhaust port may be provided between the deodorizing section.
  • the deodorizing apparatus has a blower.
  • the configuration is not limited to this, and a configuration in which the blower is removed from the configuration of the first embodiment may be adopted.
  • the deodorizing apparatus has a blower.
  • the present invention is not limited to this, and a third connection port may be formed in the input section, and the third connection port may be connected to one end surface of the blower section by a blower path to communicate with each other.
  • one end of the second ventilation path communicates with the first ventilation path.
  • the present invention is not limited to this, and one end of the second ventilation path may be connected to the input section, and the other end may be connected to the separation section.
  • the third ventilation path is provided with an intake section.
  • a deodorizing section may be provided instead of the intake section, and the intake section and the deodorizing section may be used in combination.
  • the control unit starts the operation of the suction unit and the blower unit of the deodorization device.
  • the present invention is not limited to this, and a human sensor or the like may be provided near the first lid, and the operations of the air intake unit and the air blowing unit of the deodorizing device may be started before the first lid is raised. At this time, the momentum at which the suction unit and the air blowing unit operate may be changed between immediately after the first lid is raised and after a predetermined time has elapsed after the first lid is raised. . (7)
  • the deodorizing section is disposed so as to cover the other end surface of the suction section.
  • the present invention is not limited to this, and the deodorizing section may be arranged so as to cover one end surface of the intake section.
  • Embodiment 3 of the first waste disposal apparatus the water sealing section is provided in the charging section.
  • the present invention is not limited to this, and a packing may be provided in a portion of the first lid where the charging port of the charging unit contacts.
  • the deodorizing apparatus has a deodorant and an aromatic.
  • the configuration is not limited to this, and the deodorizing device may have only one of the deodorant and the fragrance.
  • the second waste disposal apparatus is not limited to the fourth embodiment described with reference to the above description and the drawings.
  • the second embodiment may be as follows. (1) In Embodiment 4 of the second waste disposal apparatus, in the cleaning mode, the second open / close valve is closed, and hot water is stored in the processing unit except for the decomposition tank.
  • the present invention is not limited to this, and a third on-off valve and a fourth on-off valve are provided on the drainage channel on the downstream side of the decomposition tank and on the base end of the solids discharge unit. Hot water may be stored in all of the processing units by setting the second on-off valve to an open state and closing the third on-off valve and the fourth on-off valve.
  • Embodiment 4 of the second waste disposal apparatus heaters are provided in all processing units.
  • a heater may be provided in a discharge channel, a drain channel, or the like.
  • motors other than the motor of the separation unit are alternately driven in the forward direction and the reverse direction.
  • the present invention is not limited to this, and the driving speed may be changed periodically while driving the motors of all the processing units in one direction.
  • hot water is discharged from the discharge unit while driving all the processing units.
  • the present invention is not limited to this. In the cleaning mode, water may be discharged from the discharge unit while all the processing units are driven, and the discharged water may be heated by the heater.
  • the third waste disposal apparatus is not limited to the fifth embodiment described with reference to the above description and the drawings, and may be, for example, the following embodiment.
  • the first manual open / close valve is provided upstream of the first open / close valve
  • the second manual open / close valve is provided upstream of the second open / close valve.
  • the present invention is not limited to this, and a first manual open / close valve may be provided downstream of the first open / close valve, and a second manual open / close valve may be provided downstream of the second open / close valve.
  • the first sewage treatment apparatus, the second sewage treatment apparatus, and the third sewage treatment apparatus are not limited to the first, fourth, and fifth embodiments described above and illustrated in the drawings. Such an embodiment may be used.
  • CaCl 2 is used as a decomposing agent.
  • the present invention is not limited to this, and may include other components including a divalent metal salt such as Ca and Mg, for example, a water-soluble alkaline earth metal salt of calcium acetate, magnesium chloride, and magnesium nitrate.
  • a disposer is illustrated as the crushing unit.
  • the invention is not limited to this, and another device such as a grinder pump may be used as the crushing unit.
  • the decomposing agent may be solid or liquid.
  • a decomposing agent storage device that has a decomposing agent storage tank for storing the decomposing agent and a pump that takes out the decomposing agent from the decomposing agent storage tank and feeds the decomposed agent toward an input path is used.
  • Embodiment 1 of the first waste disposal apparatus, Embodiment 4 of the second waste disposal apparatus, and Embodiment 5 of the third waste disposal apparatus the discharge unit is provided in the input unit.
  • the present invention is not limited to this, and the discharge unit may be provided in the dilution tank.
  • a separation unit is provided in Embodiment 1 of the first waste disposal apparatus, Embodiment 4 of the second waste disposal apparatus, and Embodiment 5 of the third waste disposal apparatus.
  • a separation unit is provided in the case where the diluent may be allowed to flow through the sewer pipe as it is, there is no need to separate the solid content from the diluent, so that a separation unit may not be provided.
  • Embodiment 1 of the first waste disposal apparatus, Embodiment 4 of the second waste disposal apparatus, and Embodiment 5 of the third waste disposal apparatus the control unit controls the first load of the motor of the crushing unit.
  • the amount of waste input is estimated based on the size.
  • the present invention is not limited to this, and a counting unit that counts the number of filths input to the input unit may be provided, and the control unit may estimate the amount of the input filth based on a signal from the counting unit.
  • inspection is performed on the side of the dilution tank and the side of the separation unit. The mouth is formed.
  • an inspection port may be provided on the upper surface of the dilution tank and the upper surface of the separation unit.
  • the fourth waste disposal apparatus is not limited to the sixth embodiment described with reference to the above description and drawings, and may be, for example, the following embodiment.
  • the first processing agent input section for inputting the processing agent containing calcium acetate and the second processing agent input section for inputting the processing agent containing calcium chloride are provided.
  • the form which the treatment agent introduction part has is illustrated.
  • the present invention is not limited to this, and may be a form having only one treatment agent charging section.
  • one treatment agent charging section may charge a treatment agent in which calcium acetate and calcium chloride are mixed in advance, or may charge a treatment agent containing only calcium acetate. You may.
  • the control unit and the measurement unit as an information acquisition unit for acquiring information on the operation state of the processing unit were provided.
  • this configuration is not essential.
  • the information acquisition unit is provided, the information on the operation state of the processing unit to be acquired is not limited to the exemplified load reduction time, and the current consumption value measured by each measurement unit. Numerical values such as the frequency, the water level and the pressure inside the processing unit, and information other than the numerical values such as color change, abnormal noise and noise obtained based on these numerical values may be used.
  • the information acquisition unit may be a form of directly acquiring a measurement value obtained by directly measuring these numerical values, or may indirectly acquire information on the operating state of the processing unit based on information such as the measured numerical values.
  • the acquisition form may be used.
  • the form in which the determination unit predicts the state of the processing unit based on the information on the past operation state stored in the storage unit has been exemplified. However, this is not required.
  • the method is not limited to the linear regression analysis described above, but may be another method, such as another linear regression or a non-linear regression analysis.
  • the determination unit determines the state of the object to be processed based on the measurement result of the measurement unit, and based on the measurement result of the measurement unit.
  • Each of the determination modes has been exemplified.
  • the present invention is not limited to this, and the determination may be made based on one of the results, or the determination may be made based on another matter.
  • the control unit detects that the amount of the processing agent supplied from the processing agent input unit is insufficient for the state of the disposable diaper to be processed, The form in which the control for stopping the operation of the unit is executed has been exemplified. However, it is not essential in the waste disposal apparatus according to the present disclosure.
  • the fifth waste disposal apparatus is not limited to the sixth embodiment described with reference to the above description and drawings, and may be, for example, the following embodiment.
  • a form having one treatment agent charging section or a form having three or more treatment agent charging sections may be used.
  • the determination unit determines the state of the workpiece.
  • the determination is not limited to the form based on the measurement result of the exemplified measurement unit and the form based on the measurement result of the measurement unit. The determination may be based on the result, or the determination may be based on other items.
  • the present invention is not limited to these.
  • numerical values such as motor temperature, rotation speed, vibration frequency, water level and pressure inside the processing unit, and numerical values such as color change, abnormal noise and noise obtained based on these numerical values
  • Other information may be used. That is, the information acquisition unit may be a form of directly acquiring a measurement value obtained by directly measuring these numerical values, or may indirectly acquire information on the operating state of the processing unit based on information such as the measured numerical values. The acquisition form may be used.
  • a regression analysis by linear regression is exemplified as a method in which the determination unit predicts the state of the processing unit.
  • the present invention is not limited to this, and other methods such as regression analysis using linear regression or non-linear regression may be used.
  • the fourth waste disposal apparatus and the fifth waste disposal apparatus are not limited to the sixth embodiment described above with reference to the drawings, but may be, for example, the following embodiments.
  • (1) In Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, a disposable diaper was illustrated as an object to be treated. However, the present invention is not limited to this, and other objects such as sanitary products, pet sheets, pet sand, and the like may be used as the processing target.
  • the processing section includes a crushing section, a mixer, a dilution tank, and a separation section has been described.
  • the configuration of the processing unit is not limited to the embodiment.
  • a configuration that does not include a part of the processing unit described in the embodiment such as a configuration that does not include one or more of a crushing unit, a mixer, a dilution tank, and a separation unit, or a second mixer
  • a configuration having one processing unit for performing a mixing step and a dilution step instead of the two processing units of the mixer and the dilution tank may be configured to have a processing unit integrated into one.
  • the water supply unit may be provided in a processing unit such as a crushing unit, a mixer, a dilution tank, and a separation unit other than the charging unit, or a charging unit and a mixer, and a crushing unit and a mixer. It may be provided at a plurality of places such as a dilution tank.
  • a processing unit such as a crushing unit, a mixer, a dilution tank, and a separation unit other than the charging unit, or a charging unit and a mixer, and a crushing unit and a mixer. It may be provided at a plurality of places such as a dilution tank.
  • (4) In Embodiment 6 of the fourth and fifth waste disposal apparatuses an example in which the water supply unit supplies at least one of water and hot water has been described. However, the present invention is not limited to this, and only water may be used.
  • the form provided with the notification unit was exemplified.
  • the display unit is not limited to the display device that displays the characters or graphics as exemplified, but may be a buzzer or a speaker that emits a sound or a voice, or may be a combination of different types of notification units. There may be.
  • the form provided with the storage unit was exemplified. However, this is not an essential configuration in the waste disposal apparatus according to the present disclosure.
  • the sixth embodiment of the fourth and fifth waste disposal apparatuses has exemplified the form including the transmission unit. However, this is not an essential configuration in the waste disposal apparatus according to the present disclosure.
  • Embodiment 6 of the fourth filth treatment apparatus and the fifth filth treatment apparatus an example in which two types of treatment agents, that is, a treatment agent containing calcium acetate and a treatment agent containing calcium chloride, are used as treatment agents did.
  • the present invention is not limited to this, and other chemicals containing divalent metal salts such as Ca and Mg may be used, and may contain magnesium chloride, water-soluble alkaline earth metal salts of magnesium nitrate, and the like. Is also good.
  • a solid treatment agent is exemplified as the treatment agent.
  • the present invention is not limited to this, and may be a liquid.
  • the treatment agent is a liquid, a known metering pump or the like can be used as the treatment agent supply unit.
  • the state of the processing unit predicted by the determination unit is a predetermined state, that is, information on the operating state measured by the measurement unit.
  • the example in which the cleaning operation of the processing unit is executed when the current consumption value exceeds the predetermined value has been described. However, this is not essential in the waste disposal apparatus according to the present disclosure.
  • (11) In Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus an example in which the determination unit re-determines the status of the processing unit after performing the cleaning mode as the cleaning operation has been described. However, this is not essential in the waste disposal apparatus according to the present disclosure.
  • Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus an example in which a measuring unit that measures the number of objects to be treated input from the input unit is illustrated.
  • the waste disposal apparatus according to the present disclosure it is not essential for the waste disposal apparatus according to the present disclosure to include the measuring unit.
  • the form of the measurement unit is not limited to the illustrated photoelectric sensor, but may be another sensor such as a laser sensor or an image sensor.
  • the measurement target of the measurement unit may be not only the number of the objects to be processed, but also the size, weight, and the like.
  • the form in which the measuring unit measures the number of the objects to be treated has been described. However, the present invention is not limited to this.
  • the measuring unit measures the object to be processed examples include other forms such as a form in which the weight of the work is measured and a mode in which the current consumption value of a motor as a driving unit is measured. There may be.
  • the position where the measuring unit is arranged may be not only the input port of the illustrated input unit but also another position of the crushing unit, the chute, the mixer, or the like.
  • the control unit exemplifies a mode in which the processing agent of the amount determined by the control unit is introduced from the processing agent introduction unit. However, this is not required. For example, a mode in which the operator manually inputs the processing agent by notifying the input amount of the processing agent determined by the control unit by the notification unit may be employed.

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Abstract

Provided is a waste decomposition device that can prevent odors from rising in a room. A waste treatment device (1) comprises: an insertion unit (10) by which waste (D) having a polymer capable of absorbing and holding moisture is inserted; a crushing unit (20) that crushes the waste (D) to make a crushed object (C); and a deodorizing device (80) that is connected to a connection opening of the insertion unit (10) and that deodorizes the odor generated from at least one of the waste (D) and the crushed object (C).

Description

汚物処理装置Waste treatment equipment
 本開示は汚物処理装置に関するものである。 The present disclosure relates to a waste disposal apparatus.
 実用新案登録第3139358号公報には、水とポリマー分離剤と滅菌・殺菌剤が供給される分離槽と、分離槽内の処理物を攪拌する攪拌機とを備えて使用済み紙おむつからパルプ類とプラスティック類とを分離して回収する使用済み紙おむつ用分離回収装置において、分離槽に収集体に入れられた使用済み紙おむつが投入されると共に、収集体と使用済み紙おむつを破砕し得る破砕手段が設けられていることが開示されている。 Japanese Utility Model Registration No. 3139358 discloses a separation tank to which water, a polymer separating agent and a sterilizing / sterilizing agent are supplied, and a stirrer for stirring the processed material in the separation tank. In a used paper diaper separating and collecting apparatus for separating and collecting diapers, used paper diapers put in a collecting body are put into a separation tank, and crushing means for crushing the collected body and the used paper diaper are provided. Is disclosed.
 特開2018-24964号公報には使用済み吸収性物品からパルプ繊維を回収する方法が開示されている。この方法は、ホットメルトや粘着テープで表面シートと裏面シートとが固定された紙おむつにテルペンを添加した水溶液を加えることによって、ホットメルトや粘着テープを溶解させ、紙おむつの表面シートと裏面シートとを分離し、表面シートと裏面シートとの間に配置されたパルプや高分子ポリマーを取り出すことができる。 JP-A-2018-24964 discloses a method for recovering pulp fibers from used absorbent articles. This method dissolves the hot melt or the adhesive tape by adding an aqueous solution containing a terpene to a disposable diaper in which the top sheet and the back sheet are fixed with a hot melt or an adhesive tape, and forms the top sheet and the back sheet of the disposable diaper. It is possible to take out the pulp or the high-molecular polymer separated and separated between the top sheet and the back sheet.
 特開2000-84533号公報には使用済み紙おむつに使用材料の再生処理方法が開示されている。この方法を実行する再生処理設備は、紙おむつを破砕した後、ポリマー分解槽でポリマーを分解し、ビニルやパルプを回収することができる。 Japanese Patent Application Laid-Open No. 2000-84533 discloses a method of recycling used materials for used disposable diapers. The recycling equipment that performs this method can crush the paper diaper and then decompose the polymer in a polymer decomposition tank to recover vinyl and pulp.
 特開2000-84533号公報には、被処理物としての使用済み紙おむつを廃棄処理する廃棄処理設備が開示されている。この廃棄処理設備は、紙おむつと、紙おむつのポリマーに吸収された水分とを分けることができる。具体的には、紙おむつに含まれる高分子吸水ポリマーと、処理剤としてのポリマー分解剤とを反応させて、高分子吸水ポリマーから水分を取り出す。具体的には、破砕機、ポリマー分解槽、撹拌槽等において処理を行うことによって、ポリマーから水分を分離する。 JP-A-2000-84533 discloses a disposal facility for disposing of used paper diapers as an object to be treated. This disposal facility can separate the disposable diaper from the water absorbed by the disposable diaper polymer. Specifically, the high-molecular-weight water-absorbing polymer contained in the disposable diaper is reacted with a polymer-decomposing agent as a treating agent, and water is extracted from the high-molecular-weight water-absorbing polymer. Specifically, water is separated from the polymer by performing the treatment in a crusher, a polymer decomposition tank, a stirring tank, or the like.
 実用新案登録第3139358号公報の使用済み紙おむつ用破砕分離回収装置は、排せつ物を含んだ使用済み紙おむつを分離槽で処理する際、投入口から室内に臭気が立ち昇ってくるおそれがある。 In the used paper diaper crushing separation and recovery device disclosed in Utility Model Registration No. 3139358, when a used paper diaper containing excretions is treated in the separation tank, odor may rise into the room from the charging port.
 第1の汚物処理装置は、上記従来の事情に鑑みてなされたものであって、室内に臭気が立ち昇ることを抑えることができる汚物処理装置を提供することを解決すべき課題としている。 The first waste disposal apparatus has been made in view of the above-mentioned conventional circumstances, and an object of the present invention is to provide a waste disposal apparatus capable of suppressing the rise of odor in a room.
 特開2018-24964号公報の方法は、テルペンを添加する量が不足した場合、ホットメルトや粘着テープを十分に溶解することができないおそれがある。この場合、紙おむつを処理する汚物処理装置にこの方法を採用した場合、表面シートと裏面シートとの間に配置されたパルプや高分子ポリマーを取り出せないだけでなく、ホットメルトや粘着テープが処理装置内に付着してしまい、汚物処理装置が良好に動作できなくなるおそれがある。 In the method disclosed in JP-A-2018-24964, when the amount of the terpene added is insufficient, the hot melt or the adhesive tape may not be sufficiently dissolved. In this case, when this method is adopted in a waste disposal apparatus for treating a disposable diaper, not only can the pulp and the high molecular polymer disposed between the top sheet and the back sheet be taken out, but also the hot melt and the adhesive tape can be used in the treatment apparatus. And the waste may be unable to operate properly.
 第2の汚物処理装置は、上記従来の事情に鑑みてなされたものであって、良好に動作することができる汚物処理装置を提供することを解決すべき課題としている。 The second waste disposal apparatus has been made in view of the above-mentioned conventional circumstances, and has as an object to provide a waste disposal apparatus that can operate well.
 特開2000-84533号公報の方法を実行する再生処理設備は、各装置の間に設けた中継槽によって、各装置の処理量や処理時間の差異を吸収している。このため、この再生処理設備は中継槽を設けることによって大型化してしまうおそれがある。 再生 In the regeneration processing equipment that executes the method of Japanese Patent Application Laid-Open No. 2000-84533, a difference in the processing amount and processing time of each device is absorbed by a relay tank provided between the devices. For this reason, there is a possibility that the size of the reprocessing equipment may be increased by providing a relay tank.
 第3の汚物処理装置は、上記従来の事情に鑑みてなされたものであって、より小型化した汚物処理装置を提供することを解決すべき課題としている。 The third waste disposal apparatus has been made in view of the above-mentioned conventional circumstances, and has as an object to solve the problem of providing a more compact waste disposal apparatus.
 特開2000-84533号公報のような汚物処理装置において、ポリマーから水分を分離する処理に使用する処理剤の量が十分でない場合、処理剤と未反応で水分を再び吸収可能な状態のポリマーが残ってしまうといった不具合があった。一方、処理剤の量が多すぎると、処理剤の成分が装置内部で固着してしまったり、コストアップに繋がってしまったり等の不具合が生じる。 In a filth treatment apparatus as disclosed in Japanese Patent Application Laid-Open No. 2000-84533, if the amount of the treatment agent used for the treatment for separating water from the polymer is not sufficient, the polymer which has not reacted with the treatment agent and is capable of absorbing water again is used. There was a problem that it would remain. On the other hand, if the amount of the treatment agent is too large, problems such as the components of the treatment agent sticking inside the apparatus and leading to an increase in cost occur.
 第4の汚物処理装置は、上記従来の実情に鑑みてなされたものであって、処理剤の過不足による不具合の発生を抑制することができる汚物処理装置を提供することを解決すべき課題としている。 The fourth waste disposal apparatus has been made in view of the above-mentioned conventional situation, and an object of the present invention is to provide a waste disposal apparatus capable of suppressing the occurrence of problems due to excess or deficiency of the treatment agent. I have.
 特開2000-84533号公報の汚物処理装置の場合、例えば、各処理において不具合の発生するおそれが生じた場合等の状況把握は各作業者の判断に委ねられると考えられる。この場合、作業者が異なると判断結果も異なることがあるため、正確な状況を把握できないおそれがある。 汚 In the case of the waste disposal apparatus disclosed in Japanese Patent Application Laid-Open No. 2000-84533, it is considered that the grasp of the situation, for example, in the case where a problem may occur in each process, is left to the judgment of each worker. In this case, if the operator is different, the result of the determination may be different, so that an accurate situation may not be grasped.
 第5の汚物処理装置は、上記従来の実情に鑑みてなされたものであって、処理部の状況をより正確に把握することができる汚物処理装置を提供することを解決すべき課題としている。 The fifth waste disposal apparatus has been made in view of the above-described conventional situation, and has as an object to solve the problem of providing a waste disposal apparatus capable of more accurately grasping the status of the processing unit.
 第1の汚物処理装置は、水分を吸収保持可能なポリマーを有する汚物を投入する投入部と、前記汚物を破砕して破砕物にする破砕部と、前記投入部の接続口に接続され、前記汚物及び前記破砕物の少なくともいずれか一方から生じる臭気を脱臭する脱臭装置と、を備える。 The first waste treatment apparatus is connected to a charging unit that inputs a waste having a polymer capable of absorbing and retaining moisture, a crushing unit that crushes the waste to make the crushed material, and a connection port of the input unit, A deodorizing device for deodorizing odors generated from at least one of filth and the crushed material.
 第2の汚物処理装置は、水分を吸収保持可能なポリマーを有する汚物を投入する投入部と、前記汚物を分離処理する処理部と、を備え、前記汚物を分離処理する処理モードと、前記処理部を洗浄する洗浄モードとを選択的に実行することができ、前記洗浄モードの際、水及び湯の少なくともいずれか一方を吐出する吐出部を備えている。 The second filth treatment apparatus includes: an input section for inputting filth having a polymer capable of absorbing and retaining moisture; and a processing section for separating and processing the filth; a processing mode for separating and processing the filth; And a cleaning mode for cleaning the unit. The cleaning unit includes a discharge unit that discharges at least one of water and hot water in the cleaning mode.
 第3の汚物処理装置は、水分を吸収保持可能なポリマーを有する汚物を分離処理し、直列に接続された複数の処理部を備え、下流側の前記処理部が一回の処理で処理できる処理量が上流側の前記処理部が一回の処理で処理できる処理量以上である。 The third waste treatment apparatus separates waste having a polymer capable of absorbing and retaining moisture, includes a plurality of treatment units connected in series, and the treatment unit on the downstream side can be treated in one treatment. The amount is equal to or more than the processing amount that can be processed by the processing unit on the upstream side in one process.
 第4の汚物処理装置は、吸水性のポリマーを有した被処理物が投入される投入部と、前記ポリマーの吸水性能を抑制するための処理剤を用いて前記被処理物を処理する処理部と、前記投入部から投入された前記被処理物の状態を判定する判定部を有するとともに、前記判定部によって判定した前記被処理物の状態に基づいて前記処理剤の投入量を決定する制御部と、を備えている。 A fourth waste treatment apparatus includes a charging section into which a processing object having a water-absorbing polymer is charged, and a processing section configured to process the processing object using a processing agent for suppressing water absorption performance of the polymer. And a control unit that has a determination unit that determines a state of the processing object input from the input unit, and determines an input amount of the processing agent based on the state of the processing object determined by the determination unit. And
 第5の汚物処理装置は、吸水性のポリマーを有した被処理物を前記ポリマーの吸水性能を抑制するための処理剤を用いて処理を行う処理部と、前記処理部の運転状態に関する情報を取得する情報取得部と、前記情報取得部によって取得された情報を記憶する記憶部と、前記情報取得部によって取得された情報に基づいて前記処理部の状況を判定する判定部と、を備えている。 The fifth filth disposal apparatus is a processing unit that performs processing on a processing target having a water-absorbing polymer using a processing agent for suppressing the water absorbing performance of the polymer, and information on an operation state of the processing unit. An information acquisition unit to acquire, a storage unit to store information acquired by the information acquisition unit, and a determination unit to determine the status of the processing unit based on the information acquired by the information acquisition unit, I have.
図1は、第1の汚物処理装置の実施形態1の汚物処理装置の概略図であり、FIG. 1 is a schematic diagram of a waste disposal apparatus of Embodiment 1 of the first waste disposal apparatus, 図2は、第1の汚物処理装置の実施形態2の汚物処理装置の概略図であり、FIG. 2 is a schematic diagram of a waste disposal apparatus of Embodiment 2 of the first waste disposal apparatus, 図3は、第1の汚物処理装置の実施形態3の汚物処理装置の概略図であり、FIG. 3 is a schematic diagram of a waste disposal apparatus of Embodiment 3 of the first waste disposal apparatus, 図4は、第2の汚物処理装置の実施形態4の汚物処理装置の概略図であり、FIG. 4 is a schematic diagram of a waste disposal apparatus of Embodiment 4 of the second waste disposal apparatus, 図5は、第3の汚物処理装置の実施形態5の汚物処理装置の概略図であり、FIG. 5 is a schematic diagram of a waste disposal apparatus of Embodiment 3 of the third waste disposal apparatus, 図6は、第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置の概略図であり、FIG. 6 is a schematic diagram of a waste disposal apparatus of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, 図7は、第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置の制御系の構成の概略を示すブロック図であり、FIG. 7 is a block diagram schematically illustrating a configuration of a control system of the waste disposal apparatus according to Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus. 図8は、第4の汚物処理装置及び第5の汚物処理装置の実施形態6の処理部において被処理物を処理する際のモータの消費電流の変化の例を示すグラフであり、FIG. 8 is a graph showing an example of a change in current consumption of a motor when processing a processing object in a processing unit according to the sixth embodiment of the fourth waste processing apparatus and the fifth waste processing apparatus; 図9は、第4の汚物処理装置及び第5の汚物処理装置の実施形態6の処理部において被処理物を処理する際の処理回数の増加に伴う負荷低減時間の変化の例を示すグラフであり、FIG. 9 is a graph illustrating an example of a change in load reduction time accompanying an increase in the number of times of processing when processing an object to be processed in the processing unit according to the sixth embodiment of the fourth and fifth waste disposal apparatuses. Yes, 図10は、第4の汚物処理装置及び第5の汚物処理装置の実施形態6の処理部において被処理物を処理する際の処理回数の増加に伴うモータの消費電流の変化の例を示すグラフである。FIG. 10 is a graph illustrating an example of a change in current consumption of a motor with an increase in the number of times of processing when processing an object to be processed in a processing unit according to Embodiment 6 of the fourth and fifth waste processing apparatuses. It is.
<実施形態1>
 第1の汚物処理装置の実施形態1の汚物処理装置1は、汚物である使用済の紙おむつや生理用品やペット用の砂等を破砕して、下水管に排出する装置である。これら汚物は、パルプ、プラスティック、及び高吸水性ポリマー(SAP,super absorbent polymer、以下単にポリマーと表記する)等で形成されている。これら紙おむつや生理用品やペット用の砂は使用されるとパルプやポリマーが水分を吸収保持する。水分が吸収保持されたポリマーに分解剤であるCaCl2(塩化カルシウム)等を反応させると、ポリマーから水分を取り出すことができる。分解剤としてCaCl2を反応させたポリマーは再び水分を吸収保持することができない不可逆状態になる。
<First embodiment>
The waste disposal apparatus 1 of Embodiment 1 of the first waste disposal apparatus is a device that crushes used disposable diapers, sanitary products, pet sand, and the like, and discharges the waste to a sewer pipe. These wastes are formed of pulp, plastic, superabsorbent polymer (SAP, superabsorbent polymer, hereinafter simply referred to as polymer), and the like. When these disposable diapers, sanitary products, and pet sand are used, the pulp and polymer absorb and retain moisture. By reacting CaCl 2 (calcium chloride) or the like as a decomposing agent with the polymer having absorbed and retained the water, the water can be extracted from the polymer. The polymer reacted with CaCl 2 as a decomposing agent is again in an irreversible state where it cannot absorb and retain moisture.
 第1の汚物処理装置1は、図1に示すように、使用済みの紙おむつや生理用品やペット用の砂(以降、汚物Dともいう)を投入する投入口が形成された投入部10、破砕部20、シュート21、ミキサ70、排出路11、第1開閉弁12、希釈槽30、分解剤投入装置13、脱臭装置80、吐出部14、排水路15、第2開閉弁16、分離部40、第1通気路17、負圧解消部17A、第2通気路18、及び第3通気路19を備えている。 As shown in FIG. 1, the first filth disposal apparatus 1 includes an input unit 10 having an input port for inputting used paper diapers, sanitary products, and sand for pets (hereinafter, also referred to as filth D). Part 20, chute 21, mixer 70, discharge path 11, first opening / closing valve 12, dilution tank 30, decomposing agent introducing device 13, deodorizing apparatus 80, discharging section 14, drainage path 15, second opening / closing valve 16, separation section 40 , A first ventilation path 17, a negative pressure eliminating section 17A, a second ventilation path 18, and a third ventilation path 19.
 投入部10は、上下方向に延び、筒状をなし上端に開口して投入口が形成されている。投入口には投入口を開閉する第1蓋60設けられている。投入部10には、水分を吸収保持可能なポリマーを有する汚物Dを投入する。 (4) The charging section 10 extends in the up-down direction, has a cylindrical shape, and is opened at an upper end to form a charging port. The input port is provided with a first lid 60 that opens and closes the input port. The filth D having a polymer capable of absorbing and retaining moisture is charged into the charging section 10.
 破砕部20は、破砕機(例えば、公知のディスポーザーやシュレッダー)が用いられる。破砕部20の上端は投入部10の下端に連結されている。破砕部20の側面には、破砕部20を駆動するモータ20Gが取り付けられている。モータ20Gは制御部(図示せず)によって動作が制御される。破砕部20は投入部10に投入された汚物Dを破砕して破砕物Cにする。 は The crushing unit 20 uses a crusher (for example, a known disposer or shredder). The upper end of the crushing section 20 is connected to the lower end of the charging section 10. A motor 20G for driving the crushing unit 20 is attached to a side surface of the crushing unit 20. The operation of the motor 20G is controlled by a control unit (not shown). The crushing unit 20 crushes the filth D input into the input unit 10 to obtain a crushed material C.
 制御部は、例えば、マイクロコンピュータを含んだ制御回路として構成され、CPUや記憶部等を有している。制御部には操作部(図示せず)が電気的に接続されており、汚物処理装置1を使用する使用者が操作部を操作することによって、汚物処理装置1の動作を開始したり終了したりし得る構成となっている。 The control unit is configured as a control circuit including a microcomputer, for example, and has a CPU, a storage unit, and the like. An operation unit (not shown) is electrically connected to the control unit, and the user of the waste disposal apparatus 1 operates the operation unit to start or end the operation of the waste disposal apparatus 1. It has a configuration that can be used.
 破砕部20のモータ20Gには、制御部が電気的に接続されている。制御部は破砕部20のモータ20Gが消費する消費電力量の大きさを検出して、検出した消費電力量の大きさに基づいて破砕部20に係る第1負荷を検出し得る構成とされている。具体的には、破砕部20のモータ20Gが消費する消費電力量の大きさと第1負荷の大きさとは正比例しているものとして捉え、消費電力量の大きさが紙おむつの大きさに比例しているものとする。 制 御 A control unit is electrically connected to the motor 20G of the crushing unit 20. The control unit is configured to detect the amount of power consumption consumed by the motor 20G of the crushing unit 20 and detect the first load related to the crushing unit 20 based on the detected amount of power consumption. I have. Specifically, the magnitude of the power consumption consumed by the motor 20G of the crushing unit 20 and the magnitude of the first load are regarded as being directly proportional, and the magnitude of the power consumption is proportional to the size of the disposable diaper. Shall be
 シュート21は上端から下端に向けて縮径して形成された筒状をなしており、上端が破砕部20の下端に連結されている。シュート21は破砕部20から破砕物Cを後述するミキサ70に案内する。シュート21の下端には第2蓋22が設けられている。第2蓋22は、例えば、フラッパー弁等が用いられる。第2蓋22は、破砕物C等が載置されない状態ではシュート21の下端を閉鎖する。第2蓋22は、破砕物C等が載置されると、破砕物C等の重さによって垂下してシュート21の下端を解放する。第2蓋22は、載置された破砕物C等がミキサ70に流入すると、再びシュート21の下端を閉鎖する。第2蓋22はミキサ70から破砕部20や投入部10に向けて後述する攪拌物Sが飛散したり、臭気が立ち昇ったりすることを抑えることができる。 The chute 21 has a cylindrical shape formed by reducing the diameter from the upper end to the lower end, and the upper end is connected to the lower end of the crushing unit 20. The chute 21 guides the crushed material C from the crushing unit 20 to a mixer 70 described later. A second lid 22 is provided at a lower end of the chute 21. As the second lid 22, for example, a flapper valve or the like is used. The second lid 22 closes the lower end of the chute 21 when the crushed material C or the like is not placed. When the crushed material C or the like is placed, the second lid 22 hangs down by the weight of the crushed material C or the like and releases the lower end of the chute 21. The second lid 22 closes the lower end of the chute 21 again when the placed crushed material C or the like flows into the mixer 70. The second lid 22 can prevent the later-described agitated material S from being scattered from the mixer 70 toward the crushing unit 20 and the charging unit 10 and prevent the odor from rising and rising.
 ミキサ70は上端がシュート21の下端に連結されている。ミキサ70の下面には、ミキサ70を駆動するモータ70Aが取り付けられている。ミキサ70は破砕物Cと分解剤とを攪拌して攪拌物Sにする。ミキサ70のモータ70Aには、制御部が電気的に接続されている。制御部はミキサ70のモータ70Aが消費する消費電流の大きさを検出して、検出した消費電流の大きさに基づいてミキサ70に係る第2負荷を検出し得る構成とされている。具体的には、ミキサ70のモータ70Aが消費する消費電流の大きさが稼働中に所定値を上回るときに、後述するポリマーの反応が完了していないものとする。 The mixer 70 has its upper end connected to the lower end of the chute 21. On the lower surface of the mixer 70, a motor 70A for driving the mixer 70 is attached. The mixer 70 stirs the crushed material C and the decomposing agent into a stirred material S. The control unit is electrically connected to the motor 70A of the mixer 70. The control unit is configured to detect the magnitude of the current consumed by the motor 70A of the mixer 70 and to detect the second load related to the mixer 70 based on the detected magnitude of the consumed current. Specifically, when the magnitude of the current consumed by the motor 70A of the mixer 70 exceeds a predetermined value during operation, it is assumed that the polymer reaction described below has not been completed.
 排出路11は一端がミキサ70に連通している。排出路11の他端は後述する希釈槽30に連通している。第1開閉弁12は、例えば、公知の電動ボールバルブである。第1開閉弁12は排出路11の一端部側に設けられ、排出路11を開閉する。第1開閉弁12は制御部によって開閉する動作が制御される。 One end of the discharge path 11 communicates with the mixer 70. The other end of the discharge path 11 communicates with a dilution tank 30 described later. The first on-off valve 12 is, for example, a known electric ball valve. The first on-off valve 12 is provided at one end of the discharge path 11 and opens and closes the discharge path 11. The operation of opening and closing the first on-off valve 12 is controlled by the control unit.
 希釈槽30は攪拌物Sを後述する吐出部14から供給された水及び湯の少なくともいずれか一方で希釈して希釈物Tにする。希釈槽30の上面には排出路11の他端が連結されており、排出路11が希釈槽30内に連通している。希釈槽30は破砕部20の下流側に連通している。希釈槽30の上面にはモータ30Aが取り付けられている。希釈槽30内にはモータ30Aの回転軸に連結されたプロペラ(図示せず)が配置されている。希釈槽30のモータ30Aは制御部によって動作が制御される。希釈槽30の側面には点検口30Bが形成されている。点検口30Bは蓋30Cによって水密状に閉鎖されている。希釈槽30内を点検する際には、蓋30Cを外し、点検口30Bから希釈槽30内を点検する。 The diluting tank 30 dilutes the agitated material S into at least one of water and hot water supplied from the discharge unit 14 described later to obtain a diluted material T. The other end of the discharge path 11 is connected to the upper surface of the dilution tank 30, and the discharge path 11 communicates with the inside of the dilution tank 30. The dilution tank 30 communicates with the downstream side of the crushing section 20. A motor 30 </ b> A is mounted on the upper surface of the dilution tank 30. A propeller (not shown) connected to the rotation shaft of the motor 30A is disposed in the dilution tank 30. The operation of the motor 30A of the dilution tank 30 is controlled by the control unit. An inspection port 30 </ b> B is formed on a side surface of the dilution tank 30. The inspection port 30B is closed in a watertight manner by a lid 30C. When inspecting the inside of the dilution tank 30, the lid 30C is removed, and the inside of the dilution tank 30 is inspected from the inspection port 30B.
 希釈槽30のモータ30Aには、制御部が電気的に接続されている。制御部は希釈槽30のモータ30Aが消費する消費電流の大きさを検出して、検出した消費電流の大きさに基づいて希釈槽30に係る第3負荷を検出し得る構成とされている。具体的には、希釈槽30のモータ30Aが消費する消費電流の大きさが所定値を超える時に後述するポリマーの反応が完了していないものとする。 制 御 A control unit is electrically connected to the motor 30A of the dilution tank 30. The control unit is configured to detect the magnitude of the current consumed by the motor 30A of the dilution tank 30, and to detect the third load related to the dilution tank 30 based on the detected magnitude of the consumed current. Specifically, it is assumed that when the magnitude of the current consumed by the motor 30A of the dilution tank 30 exceeds a predetermined value, the reaction of the polymer described later has not been completed.
 分解剤投入装置13は分解剤をシュート21内に投入する。分解剤投入装置13は、シュート21の側面に取り付けられている。分解剤投入装置13は、例えば、公知のフィーダー等が用いられ、制御部によってシュート21に所定の量の分解剤を投入するように制御される。所定の量の分解剤の量は、汚物Dに含まれるポリマーから水分を満遍なく取り出すことができる量である。 The decomposing agent input device 13 inputs the decomposing agent into the chute 21. The decomposing agent introducing device 13 is attached to a side surface of the chute 21. For example, a known feeder or the like is used as the decomposing agent introducing device 13, and the control unit controls the chute 21 to supply a predetermined amount of the decomposing agent. The amount of the predetermined amount of the decomposing agent is an amount capable of uniformly extracting water from the polymer contained in the waste D.
 分解剤投入装置13は、制御部が電気的に接続されている。制御部は、第1負荷の大きさに対応する信号、第2負荷の大きさに対応する信号、及び第3負荷の大きさに対応する信号に基づいて分解剤を分解剤投入装置13から投入するように分解剤投入装置13を制御する。 制 御 The control unit of the decomposing agent charging device 13 is electrically connected. The control unit supplies the decomposing agent from the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, the signal corresponding to the magnitude of the second load, and the signal corresponding to the magnitude of the third load. The decomposing agent feeding device 13 is controlled so as to perform the above.
 脱臭装置80は、吸気部80A、脱臭部80B、及び送風部80Cを有している。吸気部80Aには、例えば、公知の軸流ファン等が用いられる。吸気部80Aは、一端面から吸気し、他端面から送風する。吸気部80Aは制御部に電気的に接続されている。吸気部80Aは投入部10の側面に形成された接続口である第1接続口10Dを一端面で覆うように取り付けられている。吸気部80Aは投入部10から吸気する。脱臭部80Bには、例えば、活性炭が付着した不織布等で形成された、所謂、脱臭フィルターが用いられる。脱臭部80Bは、吸気部80Aの他端面(すなわち、送風する面)を覆うように配置される。 The deodorizing device 80 has an intake unit 80A, a deodorizing unit 80B, and a blowing unit 80C. For example, a known axial fan or the like is used for the intake section 80A. The suction section 80A sucks in air from one end face and blows air from the other end face. The suction unit 80A is electrically connected to the control unit. The suction unit 80A is attached so as to cover a first connection port 10D, which is a connection port formed on a side surface of the input unit 10, with one end surface. The intake section 80A takes in air from the input section 10. For the deodorizing section 80B, for example, a so-called deodorizing filter formed of a nonwoven fabric or the like to which activated carbon is attached is used. The deodorizing section 80B is arranged so as to cover the other end face (that is, the air blowing face) of the suction section 80A.
 送風部80Cは吸気部80Aと同様の構成であり、例えば、公知の軸流ファン等が用いられる。送風部80Cは制御部に電気的に接続されている。送風部80Cは投入部10の側面に形成された接続口である第2接続口10Eを他端面で覆うように取り付けられている。投入部10は脱臭装置80を介して大気解放されている。送風部80Cは投入部10に送風する。脱臭装置80は汚物D及び破砕物Cの少なくともいずれか一方から生じる臭気を脱臭する。脱臭装置80は第1接続口10D及び第2接続口10Eに接続されている。 風 The blower unit 80C has the same configuration as the suction unit 80A, and for example, a known axial fan or the like is used. The blowing unit 80C is electrically connected to the control unit. The blowing unit 80C is attached so as to cover the second connection port 10E, which is a connection port formed on the side surface of the input unit 10, with the other end surface. The charging section 10 is open to the atmosphere via a deodorizing device 80. The blowing unit 80C blows air to the charging unit 10. The deodorizing device 80 deodorizes the odor generated from at least one of the waste D and the crushed material C. The deodorizing device 80 is connected to the first connection port 10D and the second connection port 10E.
 吐出部14は破砕部20に水及び湯の少なくともいずれか一方を供給する。吐出部14は水を供給する第1吐出部14A、及び湯を供給する第2吐出部14Bを有している。吐出部14は投入部10に設けられている。第1吐出部14A、第2吐出部14Bのそれぞれには第1電磁弁14C、第2電磁弁14Dが設けられている。 The discharge unit 14 supplies at least one of water and hot water to the crushing unit 20. The discharge unit 14 has a first discharge unit 14A that supplies water and a second discharge unit 14B that supplies hot water. The discharge unit 14 is provided in the input unit 10. A first solenoid valve 14C and a second solenoid valve 14D are provided in each of the first ejection section 14A and the second ejection section 14B.
 これら第1電磁弁14C、及び第2電磁弁14Dは制御部によって所定の条件に基づいて破砕部20に水や湯を供給するように制御される。具体的には、制御部は、破砕部20のモータ20Gの駆動が停止してからの経過時間をカウントしたり、破砕部20のモータ20Gが駆動された回数をカウントしたり、分解剤が投入された量や分解剤が投入された回数をカウントしたり、所定の時間をカウントしたりし得る構成とされている。これによって、制御部は破砕部20が動作を停止した後の所定の経過時間、破砕部20が動作した所定の回数毎、分解剤の所定の投入量毎及び所定の投入回数毎の少なくともいずれか一方、及び所定の時間毎のいずれかに、吐出部14が水及び湯の少なくともいずれか一方を供給するように制御する。これによって、破砕部20、ミキサ70、希釈槽30、分離部40を洗浄することができる。 The first solenoid valve 14C and the second solenoid valve 14D are controlled by the control unit to supply water or hot water to the crushing unit 20 based on predetermined conditions. Specifically, the control unit counts the elapsed time since the driving of the motor 20G of the crushing unit 20 is stopped, counts the number of times the motor 20G of the crushing unit 20 is driven, and inputs the disintegrant. It is configured to be able to count the amount of the disintegration agent or the number of times the disintegrant has been charged or to count a predetermined time. Thereby, the control unit determines at least one of a predetermined elapsed time after the operation of the crushing unit 20 has stopped, a predetermined number of times the crushing unit 20 has operated, a predetermined amount of the disintegrant, and a predetermined number of times of the injection. On the other hand, the discharge unit 14 is controlled so as to supply at least one of water and hot water at any one of the predetermined times. Thereby, the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 can be washed.
 排水路15は一端が希釈槽30の下端に連通して連結されている。排水路15の他端は下水管(図示せず)に連通している。排水路15にはトラップ15Aが形成されている。トラップ15Aにはゼット排水部が接続されている(図示せず。)。第2開閉弁16は、例えば、公知の電動ボールバルブである。第2開閉弁16は排水路15のトラップ15Aよりも上流側に設けられ、排水路15を開閉する。第2開閉弁16は制御部によって開閉する動作が制御される。 The drainage channel 15 is connected at one end to the lower end of the dilution tank 30. The other end of the drain 15 communicates with a sewer pipe (not shown). A trap 15 </ b> A is formed in the drainage channel 15. A jet drain section is connected to the trap 15A (not shown). The second on-off valve 16 is, for example, a known electric ball valve. The second on-off valve 16 is provided upstream of the trap 15 </ b> A of the drainage channel 15 and opens and closes the drainage channel 15. The operation of opening and closing the second on-off valve 16 is controlled by the control unit.
 分離部40はトラップ15Aと第2開閉弁16との間の排水路15に設けられている。分離部40は希釈槽30の下流側に接続されている。分離部40は、例えば、公知のスクリュープレス装置等が用いられる。分離部40の側面には、分離部40を駆動するモータ40Cが取り付けられている。分離部40の上端部には希釈物Tから分離した固形分を排出する固形分排出部40Dが連結している。分離部40は排水路15を流れる希釈物Tから固形分を分離して取り出すことができる。分離部40のモータ40Cは制御部によって動作が制御される。分離部40の側面には点検口40Aが形成されている。点検口40Aは蓋40Bによって水密状に閉鎖されている。分離部40内を点検する際には、蓋40Bを外し、点検口40Aから分離部40内を点検する。 The separation unit 40 is provided in the drainage channel 15 between the trap 15A and the second on-off valve 16. The separation section 40 is connected to the downstream side of the dilution tank 30. As the separation unit 40, for example, a known screw press device or the like is used. A motor 40C for driving the separation unit 40 is attached to a side surface of the separation unit 40. A solids discharge section 40D for discharging solids separated from the diluent T is connected to the upper end of the separation section 40. The separation section 40 can separate and extract solids from the diluent T flowing through the drainage channel 15. The operation of the motor 40C of the separation unit 40 is controlled by the control unit. An inspection port 40 </ b> A is formed on a side surface of the separation unit 40. The inspection port 40A is closed in a watertight manner by a lid 40B. When inspecting the inside of the separation unit 40, the lid 40B is removed, and the inside of the separation unit 40 is inspected from the inspection port 40A.
 第1通気路17は、一端が第1接続口10D及び第2接続口10Eよりも下流側の投入部10に連通し、他端が希釈槽30の上端に接続され、希釈槽30内に連通している。負圧解消部17Aは第1通気路17に取り付けられている。負圧解消部17Aには、例えば、公知のドルゴ通気弁やコバート通気弁等が用いられる。 One end of the first ventilation path 17 communicates with the charging section 10 downstream of the first connection port 10D and the second connection port 10E, and the other end is connected to the upper end of the dilution tank 30 and communicates with the dilution tank 30. doing. The negative pressure eliminating section 17A is attached to the first ventilation path 17. For the negative pressure eliminating section 17A, for example, a well-known Dolgo ventilation valve, a covert ventilation valve, or the like is used.
 第2通気路18は、一端が第1通気路17の負圧解消部17Aの下流側に連通して接続され、他端が分離部40の上端に連通して接続され、分離部40内に連通している。負圧解消部17Aは、第1通気路17及び第2通気路18を介して、希釈槽30内及び分離部40内の負圧を解消する。 One end of the second ventilation path 18 is connected to and connected to the downstream side of the negative pressure eliminating section 17A of the first ventilation path 17, and the other end is connected to and connected to the upper end of the separation section 40. Communicating. The negative pressure eliminating section 17A eliminates the negative pressure in the dilution tank 30 and the separation section 40 via the first ventilation path 17 and the second ventilation path 18.
 第3通気路19は、一端が投入部10の側面に連通して接続され、他端が分離部40の固形分排出部40Dに連通して接続されている。第3通気路19には、吸気部19Aが取り付けられている。吸気部19Aは、脱臭装置80の送風部80C、及び吸気部80Aと同様の構成であり、例えば、公知の軸流ファン等が用いられる。吸気部19Aは制御部に電気的に接続されている。吸気部19Aは、吸気部19Aを駆動した際に、第3通気路19内の空気が固形分排出部40Dから投入部10に向けて流れるように第3通気路19に取り付けられている。 The third ventilation path 19 has one end connected to and connected to the side surface of the charging section 10, and the other end connected to and connected to the solids discharge section 40 </ b> D of the separation section 40. An intake unit 19A is attached to the third ventilation path 19. The suction unit 19A has the same configuration as the blowing unit 80C and the suction unit 80A of the deodorizing device 80, and for example, a known axial fan or the like is used. The suction unit 19A is electrically connected to the control unit. The suction section 19A is attached to the third ventilation path 19 so that when the suction section 19A is driven, the air in the third ventilation path 19 flows from the solids discharge section 40D toward the charging section 10.
 次に、第1の汚物処理装置1の動作について説明する。
 先ず、第1蓋60を起立状態にして投入口を解放し、汚物Dを投入部10に投入する。第1蓋60を起立状態にしたことに基づいて、制御部によって脱臭装置80の吸気部80A、及び送風部80Cの動作が開始される。次に、第1蓋60を倒伏状態にして投入部10の投入口を閉鎖し、操作部(図示せず)を操作して汚物処理装置1を動作させる。
Next, the operation of the first waste disposal apparatus 1 will be described.
First, the first lid 60 is set in the upright state, the input port is opened, and the waste D is input into the input section 10. Based on the fact that the first lid 60 is in the upright state, the control unit starts the operation of the suction unit 80A and the blower unit 80C of the deodorization device 80. Next, the first lid 60 is placed in the lying state, the input port of the input unit 10 is closed, and the operation unit (not shown) is operated to operate the waste disposal apparatus 1.
 汚物処理装置1は、先ず、制御部によって第1電磁弁14C及び第2電磁弁14Dの少なくともいずれか一方を動作させて、吐出部14から第1所定量の水及び湯の少なくともいずれか一方を破砕部20に供給する。こうして、破砕部20に汚物Dと水及び湯の少なくともいずれか一方とが投入される。このとき、第1開閉弁12は閉じた状態である。破砕部20のモータ20Gは、第1蓋60が投入口を解放した状態、及び分解剤が投入されていない状態の少なくともいずれか一方の状態であると制御部が判別した場合、駆動しないように制御部によって制御されている。 The waste disposal apparatus 1 first operates at least one of the first solenoid valve 14C and the second solenoid valve 14D by the control unit to discharge at least one of the first predetermined amount of water and hot water from the discharge unit 14. It is supplied to the crushing unit 20. Thus, the filth D and at least one of water and hot water are put into the crushing unit 20. At this time, the first on-off valve 12 is in a closed state. The motor 20G of the crushing unit 20 is not driven when the control unit determines that the first lid 60 has at least one of the state in which the inlet is opened and the state in which the disintegrant is not charged. It is controlled by the control unit.
 第1蓋60が投入口を閉鎖した状態、及び分解剤が投入された状態であると制御部が判別すると、破砕部20のモータ20Gが駆動され、汚物Dが破砕される。このとき、制御部はモータ20Gの第1負荷の大きさに基づいて投入された汚物Dの量を推定する。具体的には、制御部によって、破砕部20に係る第1負荷(すなわち、モータ20Gの消費電力量)を検出し、第1負荷が所定値を超えたときに汚物Dを破砕しているものとし、第1負荷が所定値を超えている時間に基づいて汚物Dの量を推定する。汚物Dは破砕部20で破砕され破砕物Cになる。制御部は、第1負荷の大きさに対応する信号に基づいて分解剤投入装置13を動作させて、所定の量の分解剤をシュート21に投入する。シュート21に投入された所定の量の分解剤はミキサ70に流入する。 (4) When the control unit determines that the first lid 60 is in the state in which the inlet is closed and the state in which the decomposing agent is charged, the motor 20G of the crushing unit 20 is driven, and the waste D is crushed. At this time, the control unit estimates the amount of the input waste D based on the magnitude of the first load of the motor 20G. Specifically, the control unit detects the first load (that is, the power consumption of the motor 20G) related to the crushing unit 20 and crushes the waste D when the first load exceeds a predetermined value. Then, the amount of the waste D is estimated based on the time when the first load exceeds the predetermined value. The filth D is crushed in the crushing unit 20 to become the crushed material C. The control unit operates the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, and injects a predetermined amount of the decomposing agent into the chute 21. A predetermined amount of the decomposing agent supplied to the chute 21 flows into the mixer 70.
 次に、ミキサ70で、破砕物Cと、第1所定量の水及び湯の少なくともいずれか一方と、所定の量の分解剤とを攪拌して、水分を吸収保持したポリマーと分解剤とを反応させて、ポリマーが吸収保持した水分を取り出す。こうして、ミキサ70では、破砕物Cと、水及び湯の少なくともいずれか一方と、所定の量の分解剤とを攪拌して攪拌物Sにする。 Next, in the mixer 70, the crushed material C, at least one of the first predetermined amount of water and hot water, and the predetermined amount of the decomposing agent are stirred, and the polymer having absorbed and retained the water and the decomposing agent are mixed. The reaction is allowed to take out the water absorbed and retained by the polymer. In this way, in the mixer 70, the crushed material C, at least one of water and hot water, and a predetermined amount of the decomposing agent are stirred to form the stirred material S.
 このとき、制御部によって、ミキサ70のモータ70Aに係る第2負荷を検出する。具体的には、このとき検出される第2負荷の大きさは、モータ70Aの消費電流の大きさである。 At this time, the controller detects the second load related to the motor 70A of the mixer 70. Specifically, the magnitude of the second load detected at this time is the magnitude of the current consumption of the motor 70A.
 制御部はモータ70Aの第2負荷の大きさが所定の時間が経過しても所定値以下でない(すなわち、攪拌物Sのポリマーと分解剤との反応が十分進んでいない)と判別すると、分解剤を分解剤投入装置13から追加して投入するように分解剤投入装置13を制御する。このとき、モータ70Aは継続して駆動しており、ミキサ70において攪拌物Sのポリマーと分解剤との反応をさらに進めることができる。こうして、ミキサ70では、破砕物Cと、第1所定量の水及び湯の少なくともいずれか一方と、分解剤とを攪拌し、破砕物Cを攪拌物Sにし、攪拌物Sのポリマーと分解剤との反応をさらに進めることができる。 If the control unit determines that the magnitude of the second load of the motor 70A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the agitated material S and the decomposer has not sufficiently proceeded), The disintegrating agent injecting device 13 is controlled so that an agent is additionally injected from the injecting agent injecting device 13. At this time, the motor 70A is continuously driven, and the mixer 70 can further promote the reaction between the polymer of the agitated substance S and the decomposing agent. Thus, in the mixer 70, the crushed material C, at least one of the first predetermined amount of water and hot water, and the decomposing agent are agitated, and the crushed material C is converted into the agitated material S. The reaction with can be further advanced.
 次に、モータ70Aの消費電流の大きさ(すなわち、第2負荷の大きさ)が所定値以下であると制御部が判別すると、閉じた状態の第1開閉弁12が制御部によって開いた状態にされる。すると、排出路11を介して攪拌物Sが希釈槽30内に流入する。 Next, when the control unit determines that the magnitude of the current consumption of the motor 70A (that is, the magnitude of the second load) is equal to or smaller than a predetermined value, the first on-off valve 12 in the closed state is opened by the control unit. To be. Then, the agitated material S flows into the dilution tank 30 via the discharge path 11.
 このとき、制御部によって吐出部14の第1電磁弁14C及び第2電磁弁14Dを動作させて吐出部14から第2所定量の水及び湯の少なくともいずれか一方を破砕部20に供給する。第2所定量の水及び湯の少なくともいずれか一方は、攪拌物Sの量に対して所定の量である。このとき、破砕部20のモータ20G、及びミキサ70のモータ70Aは駆動している。これによって、ミキサ70内の攪拌物Sを希釈槽30内に確実に搬送しつつ破砕部20内及びミキサ70内を洗浄することができる。第1通気路17は、希釈槽30に破砕物C及び第2所定量の水及び湯の少なくともいずれか一方が流入する際、希釈槽30内が正圧になることを抑える。吐出部14から第2所定量の水及び湯の少なくともいずれか一方が供給された際に破砕部20から水及び湯の少なくともいずれか一方が溢れる場合には、第1通気路17を介して第2所定量の水及び湯の少なくともいずれか一方の一部が希釈槽30に流れる。第2開閉弁16は、第2所定量の水及び湯の少なくともいずれか一方と攪拌物Sとが希釈槽30に流入するときから閉じた状態である。 At this time, the first electromagnetic valve 14C and the second electromagnetic valve 14D of the discharge unit 14 are operated by the control unit to supply at least one of the second predetermined amount of water and hot water from the discharge unit 14 to the crushing unit 20. At least one of the second predetermined amount of water and hot water is a predetermined amount with respect to the amount of the stirring object S. At this time, the motor 20G of the crushing unit 20 and the motor 70A of the mixer 70 are being driven. Thus, the inside of the crushing unit 20 and the inside of the mixer 70 can be washed while the stirred material S in the mixer 70 is surely conveyed into the dilution tank 30. The first ventilation path 17 suppresses the inside of the dilution tank 30 from becoming a positive pressure when at least one of the crushed material C and the second predetermined amount of water and hot water flows into the dilution tank 30. If at least one of the water and the hot water overflows from the crushing unit 20 when at least one of the second predetermined amount of the water and the hot water is supplied from the discharge unit 14, the second predetermined amount is supplied through the first ventilation path 17. 2 A part of at least one of the predetermined amount of water and hot water flows into the dilution tank 30. The second on-off valve 16 is in a closed state when at least one of the second predetermined amount of water and hot water and the agitated material S flow into the dilution tank 30.
 次に、第2所定量の水及び湯の少なくともいずれか一方と攪拌物Sとを希釈槽30で希釈して攪拌物Sを希釈物Tにする。このとき、第2開閉弁16は閉じた状態である。先ず、制御部によって希釈槽30のモータ30Aの駆動が開始される。これによって、希釈槽30のプロペラ(図示せず)が回転し、第2所定量の水及び湯の少なくともいずれか一方と攪拌物Sとが攪拌され、攪拌物Sが希釈されて希釈物Tになる。これによって、攪拌物Sに含まれる分解剤のCa(カルシウム)やCl(塩素)の攪拌物Sにおける濃度を希釈物Tにすることによって小さくすることができ、下水管にCaの成分が付着して固まったり、Clによって下水管が腐食したりすることを抑えることができる。 Next, at least one of the second predetermined amount of water and hot water and the stirred material S are diluted in the dilution tank 30 to make the stirred material S a diluted material T. At this time, the second on-off valve 16 is in a closed state. First, the drive of the motor 30A of the dilution tank 30 is started by the control unit. As a result, the propeller (not shown) of the dilution tank 30 rotates, and the second predetermined amount of at least one of water and hot water and the agitated material S are agitated. Become. Accordingly, the concentration of Ca (calcium) or Cl (chlorine) of the decomposing agent contained in the agitated material S in the agitated material S can be reduced by using the diluent T, and the Ca component adheres to the sewer pipe. It is possible to suppress that the sewer pipe is corroded due to hardening or Cl.
 このとき、制御部によって、希釈槽30のモータ30Aに係る第3負荷を監視する。具体的には、このとき検出される第3負荷の大きさは、希釈槽30のモータ30Aの消費電流の大きさである。 、 At this time, the third load on the motor 30A of the dilution tank 30 is monitored by the control unit. Specifically, the magnitude of the third load detected at this time is the magnitude of the current consumption of the motor 30A of the dilution tank 30.
 制御部は、所定の時間が経過してもモータ30Aの第3負荷の大きさが所定値以下でない(すなわち、希釈物Tのポリマーと分解剤との反応が十分進んでいない)と判別すると、分解剤を分解剤投入装置13から追加して投入するように分解剤投入装置13を制御する。このとき、希釈槽30のモータ30Aも継続して駆動しており、希釈槽30において希釈物Tのポリマーと分解剤との反応をさらに進めることができる。こうして、希釈槽30では、攪拌物Sと第2所定量の水及び湯の少なくともいずれか一方とが攪拌され、攪拌物Sが希釈されてポリマーと分解剤との反応が進んだ希釈物Tになる。希釈槽30に分解剤投入口を形成し、この分解剤投入口にも分解剤投入装置13から分解剤を投入することができる構成としてもよい。これによって、分解剤を追加して投入する際に、希釈槽30に分解剤を直接投入することができる。 If the control unit determines that the magnitude of the third load of the motor 30A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the diluent T and the decomposer has not sufficiently proceeded), The decomposing agent input device 13 is controlled so that the decomposing agent is additionally input from the decomposing agent input device 13. At this time, the motor 30A of the dilution tank 30 is also continuously driven, and the reaction between the polymer of the diluent T and the decomposing agent can be further advanced in the dilution tank 30. Thus, in the dilution tank 30, the agitated material S and at least one of the second predetermined amount of water and hot water are agitated, and the agitated material S is diluted to the diluted material T in which the reaction between the polymer and the decomposing agent has progressed. Become. A configuration may be adopted in which a decomposing agent inlet is formed in the dilution tank 30 and a decomposing agent can be supplied from the decomposing agent input device 13 also to this decomposing agent inlet. Thus, when the additional decomposing agent is added, the decomposing agent can be directly injected into the dilution tank 30.
 次に、希釈物Tから固形分を分離する。先ず、制御部によって、モータ30Aの消費電流の大きさ(すなわち、第3負荷の大きさ)が所定値以下であると制御部が判別すると、閉じた状態の第2開閉弁16が制御部によって開いた状態にされる。すると、希釈物Tが希釈槽30から分離部40に向けて流れる。 Next, the solid content is separated from the diluent T. First, when the control unit determines that the magnitude of the current consumption of the motor 30A (that is, the magnitude of the third load) is equal to or smaller than a predetermined value, the control unit causes the second on-off valve 16 in the closed state to be closed. It is left open. Then, the diluent T flows from the dilution tank 30 toward the separation unit 40.
 汚物処理装置1は第1蓋60で投入口が閉鎖されている。このため、第1通気路17の負圧解消部17Aから第1通気路17内に空気を取り込むことによって希釈槽30内が負圧になることを抑え、これによって、希釈物Tを希釈槽30から分離部40に向けて良好に流すことができる。制御部によって分離部40のモータ40Cの駆動が開始される。このとき、制御部によって吸気部19Aの動作も開始される。 (4) The input port of the waste disposal apparatus 1 is closed by the first lid 60. For this reason, by taking in air from the negative pressure eliminating portion 17A of the first ventilation path 17 into the first ventilation path 17, it is possible to prevent the inside of the dilution tank 30 from becoming a negative pressure. , And can be satisfactorily flowed toward the separation section 40. The drive of the motor 40C of the separation unit 40 is started by the control unit. At this time, the operation of the suction unit 19A is also started by the control unit.
 排水路15に流入した希釈物Tは、分離部40に流入し、モータ40Cが駆動することによって、希釈物Tの固形分が固形分排出部40Dから排出される。固形分排出部40Dから排出された希釈物Tの固形分は、固形分排出部40Dの先端部に取り付けられた回収袋40Eに取り込まれる。このとき、第3通気路19及び吸気部19Aによって、固形分排出部40Dで生じる臭気が投入部10に導かれる。希釈物Tの水分はトラップ15Aを通過して下水管(図示せず)に流れる。 The diluent T that has flowed into the drainage channel 15 flows into the separation unit 40, and the solid content of the diluent T is discharged from the solid discharge unit 40D by driving the motor 40C. The solids of the diluent T discharged from the solids discharge unit 40D are taken into the collection bag 40E attached to the tip of the solids discharge unit 40D. At this time, the odor generated in the solids discharge section 40D is guided to the input section 10 by the third ventilation path 19 and the suction section 19A. The water of the diluent T flows through the trap 15A to a drain (not shown).
 分離部40は第2通気路18を介して第1通気路17に連通している。これによって、分離部40内が負圧になることが抑えられ、希釈物Tの水分を分離部40から下水管に向けて良好に流すことができる。トラップ15A内に残留する希釈物Tの水分は、トラップ15Aに接続されたゼット排水部(図示せず)からトラップ15Aに向けて水を勢いよく供給することによって下水管に確実に搬送される。 The separating section 40 is in communication with the first ventilation path 17 via the second ventilation path 18. Thereby, the inside of the separation unit 40 is suppressed from being negative pressure, and the water of the diluent T can be satisfactorily flowed from the separation unit 40 toward the sewer pipe. The water of the diluent T remaining in the trap 15A is surely conveyed to the sewer pipe by vigorously supplying water to the trap 15A from a jet drain (not shown) connected to the trap 15A.
 希釈物Tからの固形分の分離が終了した後、操作部(図示せず)を操作することによって、破砕部20、ミキサ70、希釈槽30、及び分離部40の各モータ20G,70A,30A,40Cの駆動が停止される。各モータ20G,70A,30A,40Cの駆動が停止した後、所定の時間が経過したとき、制御部は吐出部14の第2吐出部14Bから湯が供給されるように制御する。このとき、制御部によって、破砕部20、ミキサ70、希釈槽30、及び分離部40の各モータ20G,70A,30A,40Cを駆動させ、第1開閉弁12、及び第2開閉弁16開いた状態にする。これによって、汚物処理装置1は、汚物処理装置1内に汚物D、破砕物C、攪拌物S、及び希釈物T等が残らないように洗浄して、汚物処理装置1内にCaの成分が付着して固まったり、Clによって汚物処理装置1内が腐食したりすることを抑えることができる。 After the separation of the solid content from the diluent T is completed, by operating an operation unit (not shown), the motors 20G, 70A, 30A of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are operated. , 40C are stopped. When a predetermined time elapses after the driving of each of the motors 20G, 70A, 30A, and 40C is stopped, the control unit controls so that hot water is supplied from the second discharge unit 14B of the discharge unit 14. At this time, the motors 20G, 70A, 30A, and 40C of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are driven by the control unit, and the first on-off valve 12 and the second on-off valve 16 are opened. State. Accordingly, the waste disposal apparatus 1 is cleaned so that the waste D, the crushed substance C, the agitated substance S, the diluent T, and the like do not remain in the waste disposal apparatus 1, and the Ca component is contained in the waste disposal apparatus 1. It is possible to suppress adhesion and solidification, and corrosion of the inside of the waste disposal apparatus 1 by Cl.
 このように、第1の汚物処理装置1は、破砕部20で汚物Dを破砕して破砕物Cにすることができる。このとき、汚物D及び破砕物Cの少なくともいずれか一方から立ち昇る臭気を脱臭装置80で脱臭することができる。 Thus, the first filth disposal apparatus 1 can crush the filth D in the crushing unit 20 to obtain the crushed material C. At this time, the odor rising from at least one of the waste material D and the crushed material C can be deodorized by the deodorizing device 80.
 したがって、第1の汚物処理装置1は室内に臭気が立ち昇ることを抑えることができる。 Therefore, the first waste disposal apparatus 1 can suppress the rise of odor in the room.
 第1の汚物処理装置1は破砕部20の下流側に連通し、破砕物Cを水で希釈して希釈物Tにする希釈槽30と、一端が第1接続口10D及び第2接続口10Eよりも下流側に接続され、他端が希釈槽30に接続された第1通気路17とを備える。このため、希釈槽30は、希釈物Tを下流側に排出する際に負圧になることを抑えると共に、希釈槽30に破砕物C等が流入する際に正圧になることを抑えることができ、破砕物C等の流入、及び希釈物Tの排出を良好にすることができる。 The first waste disposal apparatus 1 communicates with the downstream side of the crushing unit 20, and a dilution tank 30 that dilutes the crushed material C with water to make a diluted material T, and has one end having a first connection port 10D and a second connection port 10E. And a first ventilation path 17 connected to the dilution tank 30 at the other end. For this reason, the dilution tank 30 suppresses a negative pressure when the diluent T is discharged to the downstream side, and suppresses a positive pressure when the crushed material C or the like flows into the dilution tank 30. It is possible to improve the inflow of the crushed material C and the like and the discharge of the diluted material T.
 第1の汚物処理装置1は希釈槽30の下流側に接続され、希釈物Tから固形分を分離する分離部40と、一端が第1通気路17に接続され、他端が分離部40に接続された第2通気路18とを備える。このため、分離部40は、希釈物Tから固形分を取り除いた水分を下流側に排出する際に、負圧になることを抑えることができ、希釈物Tから固形分を取り除いた水分を良好に排出することができる。 The first waste disposal apparatus 1 is connected to the downstream side of the dilution tank 30, and has a separation unit 40 that separates solids from the diluent T, one end connected to the first ventilation path 17, and the other end connected to the separation unit 40. And a second air passage 18 connected thereto. For this reason, the separation unit 40 can suppress the negative pressure when discharging the moisture from which the solid content has been removed from the diluent T to the downstream side, and can desirably remove the moisture from which the solid content has been removed from the diluent T. Can be discharged.
 第1の汚物処理装置1は投入部10を閉鎖する第1蓋60と、希釈槽30内及び分離部40内の負圧を解消する負圧解消部17Aとを備えている。このため、投入部10を第1蓋60で閉鎖することによって、希釈槽30や分離部40において、希釈物Tや希釈物Tから固形分を取り除いた水分を排出する際に負圧になり易くなる。しかし、負圧解消部17Aによって、投入部10を第1蓋60で閉鎖しても希釈槽30や分離部40が負圧になり難くすることができる。 The first waste disposal apparatus 1 includes a first lid 60 for closing the charging section 10 and a negative pressure eliminating section 17A for eliminating negative pressure in the dilution tank 30 and the separating section 40. For this reason, by closing the charging section 10 with the first lid 60, the dilution tank 30 and the separation section 40 are likely to have a negative pressure when discharging the diluent T or water obtained by removing solids from the diluent T. Become. However, the negative pressure eliminating section 17A can prevent the dilution tank 30 and the separating section 40 from becoming negative pressure even when the charging section 10 is closed with the first lid 60.
 第1の汚物処理装置1の分離部40は、希釈物Tから分離した固形分を排出する固形分排出部40Dを有し、一端が投入部10に接続され、他端が固形分排出部40Dに接続された第3通気路19を備えている。このため、固形分排出部40Dで生じる臭気を投入部10に導き、投入部10を脱臭装置80で脱臭することができる。 The separation unit 40 of the first waste disposal apparatus 1 has a solids discharge unit 40D for discharging solids separated from the diluent T, one end of which is connected to the input unit 10 and the other end of which is a solids discharge unit 40D. Is provided with a third ventilation path 19 connected to the third air passage. Therefore, the odor generated in the solids discharge section 40D can be guided to the input section 10 and the input section 10 can be deodorized by the deodorizing device 80.
 第1の汚物処理装置1の脱臭装置80は、投入部10から吸気する吸気部80A、及び投入部10に送風する送風部80Cを有している。このため、投入部10において、吸気部80Aと送風部80Cとで投入部10内の空気を循環させることによって、良好に脱臭することができる。 The deodorizing device 80 of the first waste disposal apparatus 1 has an intake unit 80A that takes in air from the charging unit 10 and a blowing unit 80C that blows air to the charging unit 10. Therefore, by circulating the air in the charging section 10 between the suction section 80A and the blowing section 80C in the charging section 10, it is possible to satisfactorily deodorize.
<実施形態2>
 第1の汚物処理装置の実施形態2の汚物処理装置2は、図2に示すように、脱臭装置180の形態が実施形態1と相違する。実施形態1と同一の構成は同一の符号を付して詳細な説明を省略する。
<Embodiment 2>
As shown in FIG. 2, the first embodiment of the waste disposal apparatus 2 according to the second embodiment is different from the first embodiment in the form of a deodorizing apparatus 180. The same components as those in the first embodiment are denoted by the same reference numerals, and detailed description thereof will be omitted.
 脱臭装置180には、例えば、公知の噴霧器等が用いられる。脱臭装置180は、臭気を消す消臭剤180Dを貯蔵する消臭剤噴霧部180F、及び芳香を生じる芳香剤180Eを貯蔵する芳香剤噴霧部180Gを有している。脱臭装置180は制御部に電気的に接続されている。消臭剤噴霧部180Fは貯蔵された消臭剤180Dを噴霧する噴霧口を第2接続口10Eに連通させるように配置される。芳香剤噴霧部180Gは貯蔵された芳香剤180Eを噴霧する噴霧口を第1接続口10Dに連通させるように配置されている。
 脱臭装置180は、例えば、第1蓋60を起立状態にしたことに基づいて、制御部によって貯蔵された消臭剤180D及び芳香剤180Eを投入部10に向けて噴霧する。
As the deodorizing device 180, for example, a known sprayer or the like is used. The deodorizing device 180 has a deodorant spraying section 180F for storing a deodorant 180D for eliminating odors, and a fragrance spraying section 180G for storing a fragrance 180E that generates fragrance. The deodorizing device 180 is electrically connected to the control unit. The deodorant spraying section 180F is arranged such that a spray port for spraying the stored deodorant 180D communicates with the second connection port 10E. The fragrance spraying section 180G is arranged such that a spray port for spraying the stored fragrance 180E communicates with the first connection port 10D.
The deodorizing device 180 sprays the deodorant 180D and the fragrance 180E stored by the control unit toward the charging unit 10 based on, for example, the first lid 60 being in the upright state.
 このように、第1の汚物処理装置2は、破砕部20で汚物Dを破砕して破砕物Cにすることができる。このとき、汚物D及び破砕物Cの少なくともいずれか一方から立ち昇る臭気を脱臭装置180で脱臭することができる。 Thus, the first filth disposal apparatus 2 can crush the filth D in the crushing unit 20 to obtain the crushed material C. At this time, the odor rising from at least one of the waste material D and the crushed material C can be deodorized by the deodorizing device 180.
 したがって、第1の汚物処理装置2も室内に臭気が立ち昇ることを抑えることができる。 Therefore, the first waste disposal apparatus 2 can also suppress the rise of odor in the room.
 第1の汚物処理装置2の脱臭装置180は、臭気を消す消臭剤180D及び芳香を生じる芳香剤180Eを有している。このため、投入部10において、良好に臭気を抑えることができる。 脱 The deodorizing device 180 of the first waste disposal device 2 has a deodorant 180D for eliminating odors and a fragrance 180E for generating fragrance. For this reason, the odor can be satisfactorily suppressed in the charging section 10.
<実施形態3>
 第1の汚物処理装置の実施形態3の汚物処理装置3は、図3に示すように、投入部110の形態、及び第1蓋160の形態が実施形態1、2と相違する。実施形態1、2と同一の構成は同一の符号を付して詳細な説明を省略する。
<Embodiment 3>
As shown in FIG. 3, the waste disposal apparatus 3 according to the third embodiment of the first waste disposal apparatus is different from the first and second embodiments in the form of the charging unit 110 and the form of the first lid 160. The same components as those in the first and second embodiments are denoted by the same reference numerals, and detailed description thereof will be omitted.
 投入部110の上端部には、水封部110Aが設けられている。水封部110Aは、投入部110の内周面から内側に向けて環状をなして延びる底部110B、及び底部110Bの内側の端から上方に筒状に立ち上がる立壁部110Cを有している。水封部110Aは、投入部110の内周面、底部110B、及び立壁部110Cで囲まれた領域に水が貯留された貯留部Pが形成されている。 水 A water sealing section 110A is provided at the upper end of the charging section 110. The water seal portion 110A has a bottom portion 110B extending in an annular shape from the inner peripheral surface of the charging portion 110 to the inside, and an upright wall portion 110C that rises cylindrically upward from an inner end of the bottom portion 110B. In the water sealing section 110A, a storage section P in which water is stored is formed in a region surrounded by an inner peripheral surface of the input section 110, a bottom section 110B, and an upright wall section 110C.
 第1蓋160は、平板状をなしており、中央部に把持部160Aが設けられている。第1蓋160は外周端から垂下して垂下壁160Bが設けられている。第1蓋160は垂下壁160Bの下側が貯留部Pに浸かるように水封部110Aに載置される。こうして第1蓋160によって投入部110を閉鎖することによって、汚物処理装置3は臭気が室内に立ち昇ることを確実に抑えることができる。 The first lid 160 has a flat plate shape, and has a grip portion 160A at the center. The first lid 160 is provided with a hanging wall 160B which hangs from an outer peripheral end. The first lid 160 is placed on the water seal portion 110A such that the lower side of the hanging wall 160B is immersed in the storage portion P. By closing the charging section 110 with the first lid 160 in this manner, the waste disposal apparatus 3 can reliably suppress the odor from rising into the room.
 このように、第1の汚物処理装置3は、破砕部20で汚物Dを破砕して破砕物Cにすることができる。このとき、汚物D及び破砕物Cの少なくともいずれか一方から立ち昇る臭気を脱臭装置180で脱臭することができる。 Thus, the first filth disposal apparatus 3 can crush the filth D in the crushing unit 20 to obtain the crushed material C. At this time, the odor rising from at least one of the waste material D and the crushed material C can be deodorized by the deodorizing device 180.
 したがって、第1の汚物処理装置3も室内に臭気が立ち昇ることを抑えることができる。 Therefore, the first filth disposal device 3 can also suppress the rise of odor in the room.
<実施形態4>
 第2の汚物処理装置の実施形態4の汚物処理装置4は、汚物である使用済の紙おむつや生理用品等を破砕して、下水管に排出する装置である。これら汚物は、パルプ、プラスティック、及び高吸水性ポリマー(SAP,super absorbent polymer、以下単にポリマーと表記する)等で形成されている。これら紙おむつや生理用品は使用されるとパルプやポリマーが水分を吸収保持する。水分が吸収保持されたポリマーに分解剤であるCaCl2(塩化カルシウム)等を反応させると、ポリマーから水分を取り出すことができる。分解剤としてCaCl2を反応させたポリマーは再び水分を吸収保持することができない不可逆状態になる。
<Embodiment 4>
The waste disposal apparatus 4 of Embodiment 4 of the second waste disposal apparatus is an apparatus for crushing used paper diapers, sanitary products, and the like, which are waste, and discharging the waste to a sewer pipe. These wastes are formed of pulp, plastic, superabsorbent polymer (SAP, superabsorbent polymer, hereinafter simply referred to as polymer), and the like. When these disposable diapers and sanitary products are used, the pulp and the polymer absorb and retain moisture. By reacting CaCl 2 (calcium chloride) or the like as a decomposing agent with the polymer having absorbed and retained the water, the water can be extracted from the polymer. The polymer reacted with CaCl 2 as a decomposing agent is again in an irreversible state where it cannot absorb and retain moisture.
 紙おむつは、一般的に、ホットメルト等で表面のシートと裏面のシートとが固定されている。さらに、パットタイプの紙おむつには、一般的に、下着等に貼り付けるために用いる粘着テープが取り付けられている。ホットメルトや粘着テープは、40℃以上に加熱すると軟化して粘着力が小さくなることが知られている。 Generally, a disposable diaper has a front sheet and a back sheet fixed by hot melt or the like. Further, a pad-type disposable diaper is generally provided with an adhesive tape used for attaching to underwear or the like. It is known that hot melts and pressure-sensitive adhesive tapes are softened when heated to 40 ° C. or higher, and have low adhesive strength.
 汚物処理装置4は、図4に示すように、使用済みの紙おむつや生理用品(以降、汚物Dともいう)を投入する投入口が形成された投入部10、破砕部20、シュート21、ミキサ70、排出路11、第1開閉弁12、希釈槽30、分解剤投入装置13、脱臭装置80、吐出部14、排水路15、第2開閉弁16、分離部40、第1通気路17、負圧解消部17A、第2通気路18、及び第3通気路19を備えている。 As shown in FIG. 4, the waste disposal apparatus 4 includes an input section 10 in which an input port for inputting used paper diapers and sanitary articles (hereinafter, also referred to as waste D) is formed, a crushing section 20, a chute 21, and a mixer 70. , Discharge path 11, first opening / closing valve 12, dilution tank 30, decomposing agent introducing device 13, deodorizing device 80, discharge section 14, drainage path 15, second opening / closing valve 16, separating section 40, first ventilation path 17, negative A pressure relief section 17A, a second ventilation path 18, and a third ventilation path 19 are provided.
 破砕部20、ミキサ70、希釈槽30、及び分離部40のそれぞれは、水分を吸収保持可能なポリマーを有する汚物Dを分離処理する処理部である。以降、破砕部20、ミキサ70、希釈槽30、及び分離部40を全ての処理部ともいう。汚物処理装置4は、汚物Dを処理する処理モードと、投入部10及び全ての処理部を洗浄する洗浄モードとを選択的に実行することができる。 Each of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 is a processing unit that separates the waste D having a polymer capable of absorbing and retaining moisture. Hereinafter, the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are also referred to as all processing units. The waste disposal apparatus 4 can selectively execute a treatment mode for treating the waste D and a washing mode for washing the input unit 10 and all the treatment units.
 投入部10は、上下方向に延び、筒状をなし上端に開口して投入口が形成されている。投入口には投入口を開閉する第1蓋60が設けられている。投入部10には、水分を吸収保持可能なポリマーを有する汚物Dを投入する。 (4) The charging section 10 extends in the up-down direction, has a cylindrical shape, and is opened at an upper end to form a charging port. The input port is provided with a first lid 60 for opening and closing the input port. The filth D having a polymer capable of absorbing and retaining moisture is charged into the charging section 10.
 破砕部20は、破砕機(例えば、公知のディスポーザーやシュレッダー)が用いられる。破砕部20の上端は投入部10の下端に連結されている。破砕部20の側面には、破砕部20を駆動するモータ20G及び、ヒーターH1が取り付けられている。モータ20Gは制御部(図示せず)によって動作が制御される。ヒーターH1は制御部によって動作が制御される。破砕部20は投入部10に投入された汚物Dを破砕して破砕物Cにする。制御部は、例えば、マイクロコンピュータを含んだ制御回路として構成され、CPUや記憶部等を有している。制御部には操作部(図示せず)が電気的に接続されており、汚物処理装置4を使用する使用者が操作部を操作することによって、汚物処理装置4の動作を開始したり終了したりし得る構成となっている。 は The crushing unit 20 uses a crusher (for example, a known disposer or shredder). The upper end of the crushing section 20 is connected to the lower end of the charging section 10. A motor 20G for driving the crushing unit 20 and a heater H1 are attached to a side surface of the crushing unit 20. The operation of the motor 20G is controlled by a control unit (not shown). The operation of the heater H1 is controlled by the control unit. The crushing unit 20 crushes the filth D input into the input unit 10 to obtain a crushed material C. The control unit is configured as a control circuit including a microcomputer, for example, and has a CPU, a storage unit, and the like. An operation unit (not shown) is electrically connected to the control unit. When a user using the waste disposal apparatus 4 operates the operation unit, the operation of the waste disposal apparatus 4 is started or terminated. It has a configuration that can be used.
 破砕部20のモータ20Gには、制御部が電気的に接続されている。制御部は破砕部20のモータ20Gが消費する消費電力量の大きさを検出して、検出した消費電力量の大きさに基づいて破砕部20に係る第1負荷を検出し得る構成とされている。具体的には、破砕部20のモータ20Gが消費する消費電力量の大きさと第1負荷の大きさとは正比例しているものとして捉え、消費電力量の大きさが紙おむつの大きさに比例しているものとする。 制 御 A control unit is electrically connected to the motor 20G of the crushing unit 20. The control unit is configured to detect the amount of power consumption consumed by the motor 20G of the crushing unit 20 and detect the first load related to the crushing unit 20 based on the detected amount of power consumption. I have. Specifically, the magnitude of the power consumption consumed by the motor 20G of the crushing unit 20 and the magnitude of the first load are regarded as being directly proportional, and the magnitude of the power consumption is proportional to the size of the disposable diaper. Shall be
 シュート21は上端から下端に向けて縮径して形成された筒状をなしており、上端が破砕部20の下端に連結されている。シュート21は破砕部20から破砕物Cを後述するミキサ70に案内する。シュート21の下端には第2蓋22が設けられている。第2蓋22は、例えば、フラッパー弁等が用いられる。第2蓋22は、破砕物C等が載置されない状態ではシュート21の下端を閉鎖する。第2蓋22は、破砕物C等が載置されると、破砕物C等の重さによって垂下してシュート21の下端を解放する。第2蓋22は、載置された破砕物C等がミキサ70に流入すると、再びシュート21の下端を閉鎖する。第2蓋22はミキサ70から破砕部20や投入部10に向けて後述する攪拌物Sが飛散したり、臭気が立ち昇ったりすることを抑えることができる。シュート21の側面にはヒーターH2が取り付けられている。ヒーターH2は制御部によって動作が制御される。 The chute 21 has a cylindrical shape formed by reducing the diameter from the upper end to the lower end, and the upper end is connected to the lower end of the crushing unit 20. The chute 21 guides the crushed material C from the crushing unit 20 to a mixer 70 described later. A second lid 22 is provided at a lower end of the chute 21. As the second lid 22, for example, a flapper valve or the like is used. The second lid 22 closes the lower end of the chute 21 when the crushed material C or the like is not placed. When the crushed material C or the like is placed, the second lid 22 hangs down by the weight of the crushed material C or the like and releases the lower end of the chute 21. The second lid 22 closes the lower end of the chute 21 again when the placed crushed material C or the like flows into the mixer 70. The second lid 22 can prevent the later-described agitated material S from being scattered from the mixer 70 toward the crushing unit 20 and the charging unit 10 and prevent the odor from rising and rising. A heater H2 is attached to a side surface of the chute 21. The operation of the heater H2 is controlled by the control unit.
 ミキサ70は上端がシュート21の下端に連結されている。ミキサ70の下面には、ミキサ70を駆動するモータ70Aが取り付けられている。ミキサ70は破砕物Cと分解剤とを攪拌して攪拌物Sにする。ミキサ70のモータ70Aには、制御部が電気的に接続されている。制御部はミキサ70のモータ70Aが消費する消費電流の大きさを検出して、検出した消費電流の大きさに基づいてミキサ70に係る第2負荷を検出し得る構成とされている。具体的には、ミキサ70のモータ70Aが消費する消費電流の大きさが稼働中に所定値を上回るときに、後述するポリマーの反応が完了していないものとする。ミキサ70の側面にはヒーターH2が取り付けられている。ヒーターH2は制御部によって動作が制御される。 The mixer 70 has its upper end connected to the lower end of the chute 21. On the lower surface of the mixer 70, a motor 70A for driving the mixer 70 is attached. The mixer 70 stirs the crushed material C and the decomposing agent into a stirred material S. The control unit is electrically connected to the motor 70A of the mixer 70. The control unit is configured to detect the magnitude of the current consumed by the motor 70A of the mixer 70 and to detect the second load related to the mixer 70 based on the detected magnitude of the consumed current. Specifically, when the magnitude of the current consumed by the motor 70A of the mixer 70 exceeds a predetermined value during operation, it is assumed that the polymer reaction described below has not been completed. A heater H2 is attached to a side surface of the mixer 70. The operation of the heater H2 is controlled by the control unit.
 排出路11は一端がミキサ70に連通している。排出路11の他端は後述する希釈槽30に連通している。第1開閉弁12は、例えば、公知の電動ボールバルブである。第1開閉弁12は排出路11の一端部側に設けられ、排出路11を開閉する。第1開閉弁12は制御部によって開閉する動作が制御される。 One end of the discharge path 11 communicates with the mixer 70. The other end of the discharge path 11 communicates with a dilution tank 30 described later. The first on-off valve 12 is, for example, a known electric ball valve. The first on-off valve 12 is provided at one end of the discharge path 11 and opens and closes the discharge path 11. The operation of opening and closing the first on-off valve 12 is controlled by the control unit.
 希釈槽30は攪拌物Sを後述する吐出部14から供給された水及び湯の少なくともいずれか一方で希釈して希釈物Tにする。希釈槽30の上面には排出路11の他端が連結されており、排出路11が希釈槽30内に連通している。希釈槽30は破砕部20の下流側に連通している。希釈槽30の上面にはモータ30Aが取り付けられている。希釈槽30内にはモータ30Aの回転軸に連結されたプロペラ(図示せず)が配置されている。希釈槽30のモータ30Aは制御部によって動作が制御される。希釈槽30の側面には点検口30Bが形成されている。点検口30Bは蓋30Cによって水密状に閉鎖されている。希釈槽30内を点検する際には、蓋30Cを外し、点検口30Bから希釈槽30内を点検する。 The diluting tank 30 dilutes the agitated material S into at least one of water and hot water supplied from the discharge unit 14 described later to obtain a diluted material T. The other end of the discharge path 11 is connected to the upper surface of the dilution tank 30, and the discharge path 11 communicates with the inside of the dilution tank 30. The dilution tank 30 communicates with the downstream side of the crushing section 20. A motor 30 </ b> A is mounted on the upper surface of the dilution tank 30. A propeller (not shown) connected to the rotation shaft of the motor 30A is disposed in the dilution tank 30. The operation of the motor 30A of the dilution tank 30 is controlled by the control unit. An inspection port 30 </ b> B is formed on a side surface of the dilution tank 30. The inspection port 30B is closed in a watertight manner by a lid 30C. When inspecting the inside of the dilution tank 30, the lid 30C is removed, and the inside of the dilution tank 30 is inspected from the inspection port 30B.
 希釈槽30のモータ30Aには、制御部が電気的に接続されている。制御部は希釈槽30のモータ30Aが消費する消費電流の大きさを検出して、検出した消費電流の大きさに基づいて希釈槽30に係る第3負荷を検出し得る構成とされている。具体的には、希釈槽30のモータ30Aが消費する消費電流の大きさが所定値を超える時に後述するポリマーの反応が完了していないものとする。希釈槽30の側面にはヒーターH3が取り付けられている。ヒーターH3は制御部によって動作が制御される。 制 御 A control unit is electrically connected to the motor 30A of the dilution tank 30. The control unit is configured to detect the magnitude of the current consumed by the motor 30A of the dilution tank 30, and to detect the third load related to the dilution tank 30 based on the detected magnitude of the consumed current. Specifically, it is assumed that when the magnitude of the current consumed by the motor 30A of the dilution tank 30 exceeds a predetermined value, the reaction of the polymer described later has not been completed. A heater H3 is attached to a side surface of the dilution tank 30. The operation of the heater H3 is controlled by the control unit.
 分解剤投入装置13は分解剤をシュート21内に投入する。分解剤投入装置13は、シュート21の側面に取り付けられている。分解剤投入装置13は、例えば、公知のフィーダー等が用いられ、制御部によってシュート21に所定の量の分解剤を投入するように制御される。所定の量の分解剤の量は、汚物Dに含まれるポリマーから水分を満遍なく取り出すことができる量である。 The decomposing agent input device 13 inputs the decomposing agent into the chute 21. The decomposing agent introducing device 13 is attached to a side surface of the chute 21. For example, a known feeder or the like is used as the decomposing agent introducing device 13, and the control unit controls the chute 21 to supply a predetermined amount of the decomposing agent. The amount of the predetermined amount of the decomposing agent is an amount capable of uniformly extracting water from the polymer contained in the waste D.
 分解剤投入装置13は、制御部が電気的に接続されている。制御部は、第1負荷の大きさに対応する信号、第2負荷の大きさに対応する信号、及び第3負荷の大きさに対応する信号に基づいて分解剤を分解剤投入装置13から投入するように分解剤投入装置13を制御する。 制 御 The control unit of the decomposing agent charging device 13 is electrically connected. The control unit supplies the decomposing agent from the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, the signal corresponding to the magnitude of the second load, and the signal corresponding to the magnitude of the third load. The decomposing agent feeding device 13 is controlled so as to perform the above.
 脱臭装置80は、吸気部80A、脱臭部80B、及び送風部80Cを有している。吸気部80Aには、例えば、公知の軸流ファン等が用いられる。吸気部80Aは、一端面から吸気し、他端面から送風する。吸気部80Aは制御部に電気的に接続されている。吸気部80Aは投入部10の側面に形成された第1接続口10Dを一端面で覆うように取り付けられている。吸気部80Aは投入部10から吸気する。脱臭部80Bには、例えば、活性炭が付着した不織布等で形成された、所謂、脱臭フィルターが用いられる。脱臭部80Bは、吸気部80Aの他端面(すなわち、送風する面)を覆うように配置される。 The deodorizing device 80 has an intake unit 80A, a deodorizing unit 80B, and a blowing unit 80C. For example, a known axial fan or the like is used for the intake section 80A. The suction section 80A sucks in air from one end face and blows air from the other end face. The suction unit 80A is electrically connected to the control unit. The suction unit 80A is attached so as to cover the first connection port 10D formed on the side surface of the insertion unit 10 with one end surface. The intake section 80A takes in air from the input section 10. For the deodorizing section 80B, for example, a so-called deodorizing filter formed of a nonwoven fabric or the like to which activated carbon is attached is used. The deodorizing section 80B is arranged so as to cover the other end face (that is, the air blowing face) of the suction section 80A.
 送風部80Cは吸気部80Aと同様の構成であり、例えば、公知の軸流ファン等が用いられる。送風部80Cは制御部に電気的に接続されている。送風部80Cは投入部10の側面に形成された第2接続口10Eを他端面で覆うように取り付けられている。投入部10は脱臭装置80を介して大気解放されている。送風部80Cは投入部10に送風する。脱臭装置80は汚物D及び破砕物Cの少なくともいずれか一方から生じる臭気を脱臭する。脱臭装置80は第1接続口10D及び第2接続口10Eに接続されている。 風 The blower unit 80C has the same configuration as the suction unit 80A, and for example, a known axial fan or the like is used. The blowing unit 80C is electrically connected to the control unit. The blowing unit 80C is attached so as to cover the second connection port 10E formed on the side surface of the charging unit 10 with the other end surface. The charging section 10 is open to the atmosphere via a deodorizing device 80. The blowing unit 80C blows air to the charging unit 10. The deodorizing device 80 deodorizes the odor generated from at least one of the waste D and the crushed material C. The deodorizing device 80 is connected to the first connection port 10D and the second connection port 10E.
 吐出部14は破砕部20に水及び湯の少なくともいずれか一方を供給する。吐出部14は水を供給する第1吐出部14A、及び湯を供給する第2吐出部14Bを有している。吐出部14は投入部10に設けられている。第1吐出部14A、第2吐出部14Bのそれぞれには第1電磁弁14C、第2電磁弁14Dが設けられている。第2吐出部14Bから吐出される湯の温度は40℃から90℃である。 The discharge unit 14 supplies at least one of water and hot water to the crushing unit 20. The discharge unit 14 has a first discharge unit 14A that supplies water and a second discharge unit 14B that supplies hot water. The discharge unit 14 is provided in the input unit 10. A first solenoid valve 14C and a second solenoid valve 14D are provided in each of the first ejection section 14A and the second ejection section 14B. The temperature of the hot water discharged from the second discharge portion 14B is 40 ° C to 90 ° C.
 これら第1電磁弁14C、及び第2電磁弁14Dは全ての処理部を洗浄する洗浄モードの際、制御部によって所定の条件に基づいて破砕部20に水や湯を供給するように制御される。具体的には、制御部は、破砕部20のモータ20Gの駆動が停止してからの経過時間をカウントしたり、破砕部20のモータ20Gが駆動された回数をカウントしたり、分解剤が投入された量や分解剤が投入された回数をカウントしたり、所定の時間をカウントしたりし得る構成とされている。これによって、汚物処理装置4は全ての処理部を洗浄する洗浄モードの際、破砕部20が動作を停止した後の所定の経過時間、破砕部20が動作した所定の回数毎、分解剤の所定の投入量毎及び所定の投入回数毎の少なくともいずれか一方、及び所定の時間毎のいずれかに、吐出部14が水及び湯の少なくともいずれか一方を供給するように制御部が制御する。これによって、破砕部20、ミキサ70、希釈槽30、分離部40を洗浄することができる。つまり、吐出部14は定期的に水及び湯の少なくともいずれか一方を吐出して全ての処理部を洗浄する。 The first solenoid valve 14C and the second solenoid valve 14D are controlled by the control unit to supply water or hot water to the crushing unit 20 based on predetermined conditions in the cleaning mode for cleaning all the processing units. . Specifically, the control unit counts the elapsed time since the driving of the motor 20G of the crushing unit 20 is stopped, counts the number of times the motor 20G of the crushing unit 20 is driven, and inputs the disintegrant. It is configured to be able to count the amount of the disintegration agent or the number of times the disintegrant has been charged or to count a predetermined time. Thereby, in the cleaning mode in which all the processing sections are cleaned, the waste disposal apparatus 4 performs the predetermined time elapsed after the operation of the crushing section 20 has stopped, the predetermined number of times the crushing section 20 has operated, and the predetermined amount of the decomposing agent. The control unit controls the discharge unit 14 to supply at least one of water and hot water for at least one of the charging amount and the predetermined number of charging times and for the predetermined time period. Thereby, the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 can be washed. That is, the discharge unit 14 periodically discharges at least one of water and hot water to clean all the processing units.
 排水路15は一端が希釈槽30の下端に連通して連結されている。排水路15の他端は下水管(図示せず)に連通している。排水路15にはトラップ15Aが形成されている。トラップ15Aにはゼット排水部が接続されている(図示せず。)。第2開閉弁16は、例えば、公知の電動ボールバルブである。第2開閉弁16は排水路15のトラップ15Aよりも上流側に設けられ、排水路15を開閉する。第2開閉弁16は制御部によって開閉する動作が制御される。 The drainage channel 15 is connected at one end to the lower end of the dilution tank 30. The other end of the drain 15 communicates with a sewer pipe (not shown). A trap 15 </ b> A is formed in the drainage channel 15. A jet drain section is connected to the trap 15A (not shown). The second on-off valve 16 is, for example, a known electric ball valve. The second on-off valve 16 is provided upstream of the trap 15 </ b> A of the drainage channel 15 and opens and closes the drainage channel 15. The operation of opening and closing the second on-off valve 16 is controlled by the control unit.
 分離部40はトラップ15Aと第2開閉弁16との間の排水路15に設けられている。分離部40は希釈槽30の下流側に接続されている。分離部40は、例えば、公知のスクリュープレス装置等が用いられる。分離部40の側面には、分離部40を駆動するモータ40Cが取り付けられている。分離部40の上端部には希釈物Tから分離した固形分を排出する固形分排出部40Dが連結している。分離部40は排水路15を流れる希釈物Tから固形分を分離して取り出すことができる。分離部40のモータ40Cは制御部によって動作が制御される。分離部40の側面には点検口40Aが形成されている。点検口40Aは蓋40Bによって水密状に閉鎖されている。分離部40内を点検する際には、蓋40Bを外し、点検口40Aから分離部40内を点検する。分離部40の側面にはヒーターH4が取り付けられている。ヒーターH4は制御部によって動作が制御される。 The separation unit 40 is provided in the drainage channel 15 between the trap 15A and the second on-off valve 16. The separation section 40 is connected to the downstream side of the dilution tank 30. As the separation unit 40, for example, a known screw press device or the like is used. A motor 40C for driving the separation unit 40 is attached to a side surface of the separation unit 40. A solids discharge section 40D for discharging solids separated from the diluent T is connected to the upper end of the separation section 40. The separation section 40 can separate and extract solids from the diluent T flowing through the drainage channel 15. The operation of the motor 40C of the separation unit 40 is controlled by the control unit. An inspection port 40 </ b> A is formed on a side surface of the separation unit 40. The inspection port 40A is closed in a watertight manner by a lid 40B. When inspecting the inside of the separation unit 40, the lid 40B is removed, and the inside of the separation unit 40 is inspected from the inspection port 40A. A heater H4 is attached to a side surface of the separation unit 40. The operation of the heater H4 is controlled by the control unit.
 第2開閉弁16は希釈槽30と分離部40との間に設けられており、全ての処理部の内の下流側の2つの処理部(希釈槽30、及び分離部40)の間に設けられている。 The second on-off valve 16 is provided between the dilution tank 30 and the separation unit 40, and is provided between two downstream processing units (the dilution tank 30 and the separation unit 40) among all the processing units. Have been.
 第1通気路17は、一端が第1接続口10D及び第2接続口10Eよりも下流側の投入部10に連通し、他端が希釈槽30の上端に接続され、希釈槽30内に連通している。負圧解消部17Aは第1通気路17に取り付けられている。負圧解消部17Aには、例えば、公知のドルゴ通気弁やコバート通気弁等が用いられる。 One end of the first ventilation path 17 communicates with the charging section 10 downstream of the first connection port 10D and the second connection port 10E, and the other end is connected to the upper end of the dilution tank 30 and communicates with the dilution tank 30. doing. The negative pressure eliminating section 17A is attached to the first ventilation path 17. For the negative pressure eliminating section 17A, for example, a well-known Dolgo ventilation valve, a covert ventilation valve, or the like is used.
 第2通気路18は、一端が第1通気路17の負圧解消部17Aの下流側に連通して接続され、他端が分離部40の上端に連通して接続され、分離部40内に連通している。負圧解消部17Aは、第1通気路17及び第2通気路18を介して、希釈槽30内及び分離部40内の負圧を解消する。 One end of the second ventilation path 18 is connected to and connected to the downstream side of the negative pressure eliminating section 17A of the first ventilation path 17, and the other end is connected to and connected to the upper end of the separation section 40. Communicating. The negative pressure eliminating section 17A eliminates the negative pressure in the dilution tank 30 and the separation section 40 via the first ventilation path 17 and the second ventilation path 18.
 第3通気路19は、一端が投入部10の側面に連通して接続され、他端が分離部40の固形分排出部40Dに連通して接続されている。第3通気路19には、吸気部19Aが取り付けられている。吸気部19Aは、脱臭装置80の送風部80C、及び吸気部80Aと同様の構成であり、例えば、公知の軸流ファン等が用いられる。吸気部19Aは制御部に電気的に接続されている。吸気部19Aは、吸気部19Aを駆動した際に、第3通気路19内の空気が固形分排出部40Dから投入部10に向けて流れるように第3通気路19に取り付けられている。 The third ventilation path 19 has one end connected to and connected to the side surface of the charging section 10, and the other end connected to and connected to the solids discharge section 40 </ b> D of the separation section 40. An intake unit 19A is attached to the third ventilation path 19. The suction unit 19A has the same configuration as the blowing unit 80C and the suction unit 80A of the deodorizing device 80, and for example, a known axial fan or the like is used. The suction unit 19A is electrically connected to the control unit. The suction section 19A is attached to the third ventilation path 19 so that when the suction section 19A is driven, the air in the third ventilation path 19 flows from the solids discharge section 40D toward the charging section 10.
 次に、第2の汚物処理装置4の動作について説明する。 Next, the operation of the second waste disposal apparatus 4 will be described.
 先ず、汚物処理装置4が汚物Dを分離処理する処理モードの動作について説明する。先ず、第1蓋60を起立状態にして投入口を解放し、汚物Dを投入部10に投入する。第1蓋60を起立状態にしたことに基づいて、制御部によって脱臭装置80の吸気部80A、及び送風部80Cの動作が開始される。次に、第1蓋60を倒伏状態にして投入部10の投入口を閉鎖し、操作部(図示せず)を操作して汚物処理装置4を動作させる。 First, the operation in the processing mode in which the waste disposal apparatus 4 separates the waste D will be described. First, the first lid 60 is set in the upright state, the input port is opened, and the waste D is input into the input section 10. Based on the fact that the first lid 60 is in the upright state, the control unit starts the operation of the suction unit 80A and the blower unit 80C of the deodorization device 80. Next, the first lid 60 is placed in the lying state, the input port of the input section 10 is closed, and the operation section (not shown) is operated to operate the waste disposal apparatus 4.
 汚物処理装置4は、先ず、制御部によって第1電磁弁14C及び第2電磁弁14Dの少なくともいずれか一方を動作させて、吐出部14から第1所定量の水及び湯の少なくともいずれか一方を破砕部20に供給する。こうして、破砕部20に汚物Dと水及び湯の少なくともいずれか一方とが投入される。このとき、第1開閉弁12は閉じた状態である。破砕部20のモータ20Gは、第1蓋60が投入口を解放した状態、及び分解剤が投入されていない状態の少なくともいずれか一方の状態であると制御部が判別した場合、駆動しないように制御部によって制御されている。 The waste disposal device 4 first operates at least one of the first solenoid valve 14C and the second solenoid valve 14D by the control unit to remove at least one of the first predetermined amount of water and hot water from the discharge unit 14. It is supplied to the crushing unit 20. Thus, the filth D and at least one of water and hot water are put into the crushing unit 20. At this time, the first on-off valve 12 is in a closed state. The motor 20G of the crushing unit 20 is not driven when the control unit determines that the first lid 60 has at least one of the state in which the inlet is opened and the state in which the disintegrant is not charged. It is controlled by the control unit.
 第1蓋60が投入口を閉鎖した状態、及び分解剤が投入された状態であると制御部が判別すると、破砕部20のモータ20Gが駆動され、汚物Dが破砕される。このとき、制御部はモータ20Gの第1負荷の大きさに基づいて投入された汚物Dの量を推定する。具体的には、制御部によって、破砕部20に係る第1負荷(すなわち、モータ20Gの消費電力量)を検出し、第1負荷が所定値を超えたときに汚物Dを破砕しているものとし、第1負荷が所定値を超えている時間に基づいて汚物Dの量を推定する。汚物Dは破砕部20で破砕され破砕物Cになる。制御部は、第1負荷の大きさに対応する信号に基づいて分解剤投入装置13を動作させて、所定の量の分解剤をシュート21に投入する。シュート21に投入された分解剤はミキサ70に流入する。 (4) When the control unit determines that the first lid 60 is in the state in which the inlet is closed and the state in which the decomposing agent is charged, the motor 20G of the crushing unit 20 is driven, and the waste D is crushed. At this time, the control unit estimates the amount of the input waste D based on the magnitude of the first load of the motor 20G. Specifically, the control unit detects the first load (that is, the power consumption of the motor 20G) related to the crushing unit 20 and crushes the waste D when the first load exceeds a predetermined value. Then, the amount of the waste D is estimated based on the time when the first load exceeds the predetermined value. The filth D is crushed in the crushing unit 20 to become the crushed material C. The control unit operates the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, and injects a predetermined amount of the decomposing agent into the chute 21. The decomposing agent charged into the chute 21 flows into the mixer 70.
 次に、ミキサ70で、破砕物Cと、第1所定量の水及び湯の少なくともいずれか一方と、分解剤とを攪拌して、水分を吸収保持したポリマーと分解剤とを反応させて、ポリマーが吸収保持した水分を取り出す。こうして、ミキサ70では、破砕物Cと、水及び湯の少なくともいずれか一方と、分解剤とを攪拌して攪拌物Sにする。 Next, in the mixer 70, the crushed material C, at least one of the first predetermined amount of water and hot water, and the decomposing agent are stirred, and the polymer that has absorbed and held the water and the decomposing agent are reacted, The water absorbed by the polymer is taken out. Thus, in the mixer 70, the crushed material C, at least one of water and hot water, and the decomposing agent are agitated into the agitated material S.
 このとき、制御部によって、ミキサ70のモータ70Aに係る第2負荷を検出する。具体的には、このとき検出される第2負荷の大きさは、モータ70Aの消費電流の大きさである。 At this time, the controller detects the second load related to the motor 70A of the mixer 70. Specifically, the magnitude of the second load detected at this time is the magnitude of the current consumption of the motor 70A.
 制御部はモータ70Aの第2負荷の大きさが所定の時間が経過しても所定値以下でない(すなわち、攪拌物Sのポリマーと分解剤との反応が十分進んでいない)と判別すると、分解剤を分解剤投入装置13から追加して投入するように分解剤投入装置13を制御する。このとき、モータ70Aは継続して駆動しており、ミキサ70において攪拌物Sのポリマーと分解剤との反応をさらに進めることができる。こうして、ミキサ70では、破砕物Cと、第1所定量の水及び湯の少なくともいずれか一方と、及び分解剤とを攪拌し、破砕物Cを攪拌物Sにし、攪拌物Sのポリマーと分解剤との反応をさらに進めることができる。 If the control unit determines that the magnitude of the second load of the motor 70A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the agitated product S and the decomposing agent has not sufficiently proceeded), the control unit decomposes. The disintegrating agent injecting device 13 is controlled so that an agent is additionally injected from the injecting agent injecting device 13. At this time, the motor 70A is continuously driven, and the mixer 70 can further promote the reaction between the polymer of the agitated substance S and the decomposing agent. Thus, in the mixer 70, the crushed material C, at least one of the first predetermined amount of water and hot water, and the decomposing agent are stirred, and the crushed material C is converted into the agitated material S, and the polymer of the agitated material S is decomposed. The reaction with the agent can proceed further.
 次に、モータ70Aの消費電流の大きさ(すなわち、第2負荷の大きさ)が所定値以下であると制御部が判別すると、閉じた状態の第1開閉弁12が制御部によって開いた状態にされる。すると、排出路11を介して攪拌物Sが希釈槽30内に流入する。 Next, when the control unit determines that the magnitude of the current consumption of the motor 70A (that is, the magnitude of the second load) is equal to or smaller than a predetermined value, the first on-off valve 12 in the closed state is opened by the control unit. To be. Then, the agitated material S flows into the dilution tank 30 via the discharge path 11.
 このとき、制御部によって吐出部14の第1電磁弁14C及び第2電磁弁14Dを動作させて吐出部14から第2所定量の水及び湯の少なくともいずれか一方を破砕部20に供給する。第2所定量の水及び湯の少なくともいずれか一方は、攪拌物Sの量に対して所定の量である。このとき、破砕部20のモータ20G、及びミキサ70のモータ70Aは駆動している。これによって、ミキサ70内の攪拌物Sを希釈槽30内に確実に搬送しつつ破砕部20内及びミキサ70内を洗浄することができる。第1通気路17は、希釈槽30に破砕物C及び第2所定量の水及び湯の少なくともいずれか一方が流入する際、希釈槽30内が正圧になることを抑える。第2開閉弁16は、第2所定量の水及び湯の少なくともいずれか一方と攪拌物Sとが希釈槽30に流入するときから閉じた状態である。 At this time, the first electromagnetic valve 14C and the second electromagnetic valve 14D of the discharge unit 14 are operated by the control unit to supply at least one of the second predetermined amount of water and hot water from the discharge unit 14 to the crushing unit 20. At least one of the second predetermined amount of water and hot water is a predetermined amount with respect to the amount of the stirring object S. At this time, the motor 20G of the crushing unit 20 and the motor 70A of the mixer 70 are being driven. Thus, the inside of the crushing unit 20 and the inside of the mixer 70 can be washed while the stirred material S in the mixer 70 is surely conveyed into the dilution tank 30. The first ventilation path 17 suppresses the inside of the dilution tank 30 from becoming a positive pressure when at least one of the crushed material C and the second predetermined amount of water and hot water flows into the dilution tank 30. The second on-off valve 16 is in a closed state when at least one of the second predetermined amount of water and hot water and the agitated material S flow into the dilution tank 30.
 次に、第2所定量の水及び湯の少なくともいずれか一方と攪拌物Sとを希釈槽30で希釈して攪拌物Sを希釈物Tにする。このとき、第2開閉弁16は閉じた状態である。先ず、制御部によって希釈槽30のモータ30Aの駆動が開始される。これによって、希釈槽30のプロペラ(図示せず)が回転し、第2所定量の水及び湯の少なくともいずれか一方と攪拌物Sとが攪拌され、攪拌物Sが希釈されて希釈物Tになる。これによって、攪拌物Sに含まれる分解剤のCa(カルシウム)やCl(塩素)の攪拌物Sにおける濃度を希釈物Tにすることによって小さくすることができ、下水管にCaの成分が付着して固まったり、Clによって下水管が腐食したりすることを抑えることができる。 Next, at least one of the second predetermined amount of water and hot water and the stirred material S are diluted in the dilution tank 30 to make the stirred material S a diluted material T. At this time, the second on-off valve 16 is in a closed state. First, the drive of the motor 30A of the dilution tank 30 is started by the control unit. As a result, the propeller (not shown) of the dilution tank 30 rotates, and the second predetermined amount of at least one of water and hot water and the agitated material S are agitated. Become. Accordingly, the concentration of Ca (calcium) or Cl (chlorine) of the decomposing agent contained in the agitated material S in the agitated material S can be reduced by using the diluent T, and the Ca component adheres to the sewer pipe. It is possible to suppress that the sewer pipe is corroded due to hardening or Cl.
 このとき、制御部によって、希釈槽30のモータ30Aに係る第3負荷を監視する。具体的には、このとき検出される第3負荷の大きさは、希釈槽30のモータ30Aの消費電流の大きさである。 、 At this time, the third load on the motor 30A of the dilution tank 30 is monitored by the control unit. Specifically, the magnitude of the third load detected at this time is the magnitude of the current consumption of the motor 30A of the dilution tank 30.
 制御部は、所定の時間が経過してもモータ30Aの第3負荷の大きさが所定値以下でない(すなわち、希釈物Tのポリマーと分解剤との反応が十分進んでいない)と判別すると、分解剤を分解剤投入装置13から追加して投入するように分解剤投入装置13を制御する。このとき、希釈槽30のモータ30Aも継続して駆動しており、希釈槽30において希釈物Tのポリマーと分解剤との反応をさらに進めることができる。こうして、希釈槽30では、攪拌物Sと第2所定量の水及び湯の少なくともいずれか一方とが攪拌され、攪拌物Sが希釈されてポリマーと分解剤との反応が進んだ希釈物Tになる。希釈槽30に分解剤投入口を形成し、この分解剤投入口にも分解剤投入装置13から分解剤を投入することができる構成としてもよい。これによって、分解剤を追加して投入する際に、希釈槽30に分解剤を直接投入することができる。 If the control unit determines that the magnitude of the third load of the motor 30A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the diluent T and the decomposer has not sufficiently proceeded), The decomposing agent input device 13 is controlled so that the decomposing agent is additionally input from the decomposing agent input device 13. At this time, the motor 30A of the dilution tank 30 is also continuously driven, and the reaction between the polymer of the diluent T and the decomposing agent can be further advanced in the dilution tank 30. Thus, in the dilution tank 30, the agitated material S and at least one of the second predetermined amount of water and hot water are agitated, and the agitated material S is diluted to the diluted material T in which the reaction between the polymer and the decomposing agent has progressed. Become. A configuration may be adopted in which a decomposing agent inlet is formed in the dilution tank 30 and a decomposing agent can be supplied from the decomposing agent input device 13 also to this decomposing agent inlet. Thus, when the additional decomposing agent is added, the decomposing agent can be directly injected into the dilution tank 30.
 次に、希釈物Tから固形分を分離する。先ず、制御部によって、モータ30Aの消費電流の大きさ(すなわち、第3負荷の大きさ)が所定値以下であると制御部が判別すると、閉じた状態の第2開閉弁16が制御部によって開いた状態にされる。すると、希釈物Tが希釈槽30から分離部40に向けて流れる。 Next, the solid content is separated from the diluent T. First, when the control unit determines that the magnitude of the current consumption of the motor 30A (that is, the magnitude of the third load) is equal to or smaller than a predetermined value, the control unit causes the second on-off valve 16 in the closed state to be closed. It is left open. Then, the diluent T flows from the dilution tank 30 toward the separation unit 40.
 汚物処理装置4は第1蓋60で投入口が閉鎖されている。このため、第1通気路17の負圧解消部17Aから第1通気路17内に空気を取り込むことによって希釈槽30内が負圧になることを抑え、これによって、希釈物Tを希釈槽30から分離部40に向けて良好に流すことができる。制御部によって分離部40のモータ40Cの駆動が開始される。このとき、制御部によって吸気部19Aの動作も開始される。 (4) The input port of the waste disposal apparatus 4 is closed by the first lid 60. For this reason, by taking in air from the negative pressure eliminating portion 17A of the first ventilation path 17 into the first ventilation path 17, it is possible to prevent the inside of the dilution tank 30 from becoming a negative pressure. , And can be satisfactorily flowed toward the separation section 40. The drive of the motor 40C of the separation unit 40 is started by the control unit. At this time, the operation of the suction unit 19A is also started by the control unit.
 排水路15に流入した希釈物Tは、分離部40に流入し、モータ40Cが駆動することによって、希釈物Tの固形分が固形分排出部40Dから排出される。固形分排出部40Dから排出された希釈物Tの固形分は、固形分排出部40Dの先端部に取り付けられた回収袋40Eに取り込まれる。このとき、第3通気路19及び吸気部19Aによって、固形分排出部40Dで生じる臭気が投入部10に導かれる。希釈物Tの水分はトラップ15Aを通過して下水管(図示せず)に流れる。 The diluent T that has flowed into the drainage channel 15 flows into the separation unit 40, and the solid content of the diluent T is discharged from the solid discharge unit 40D by driving the motor 40C. The solids of the diluent T discharged from the solids discharge unit 40D are taken into the collection bag 40E attached to the tip of the solids discharge unit 40D. At this time, the odor generated in the solids discharge section 40D is guided to the input section 10 by the third ventilation path 19 and the suction section 19A. The water of the diluent T flows through the trap 15A to a drain (not shown).
 分離部40は第2通気路18を介して第1通気路17に連通している。これによって、分離部40内が負圧になることが抑えられ、希釈物Tの水分を分離部40から下水管に向けて良好に流すことができる。トラップ15A内に残留する希釈物Tの水分は、トラップ15Aに接続されたゼット排水部(図示せず)からトラップ15Aに向けて水を勢いよく供給することによって下水管に確実に搬送される。 The separating section 40 is in communication with the first ventilation path 17 via the second ventilation path 18. Thereby, the inside of the separation unit 40 is suppressed from being negative pressure, and the water of the diluent T can be satisfactorily flowed from the separation unit 40 toward the sewer pipe. The water of the diluent T remaining in the trap 15A is reliably transported to the sewer pipe by vigorously supplying water to the trap 15A from a jet drain (not shown) connected to the trap 15A.
 希釈物Tからの固形分の分離が終了した後、操作部(図示せず)を操作することによって、破砕部20、ミキサ70、希釈槽30、及び分離部40の各モータ20G,70A,30A,40Cの駆動が停止される。こうして、処理モードが終了する。 After the separation of the solid content from the diluent T is completed, by operating an operation unit (not shown), the motors 20G, 70A, 30A of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are operated. , 40C are stopped. Thus, the processing mode ends.
次に、汚物処理装置4が投入部10及び全ての処理部を洗浄する洗浄モードの動作について説明する。各モータ20G,70A,30A,40Cの駆動が停止した後、所定の時間が経過したとき、制御部は吐出部14の第2吐出部14Bから湯が供給されるように制御する。吐出部14は洗浄モードの際に投入部10に湯を吐出する。このとき、汚物処理装置4は、制御部によって、各モータ20G,70A,30A,40Cを駆動させ、第1開閉弁12を開いた状態にし、第2開閉弁16を閉じた状態にする。つまり、汚物処理装置4は洗浄モードの際、全ての処理部を駆動させつつ、吐出部14から湯を吐出する。これによって、汚物処理装置4は、洗浄モードの際に第2開閉弁16を閉じて破砕部20、ミキサ70、及び希釈槽30(以降、分離部40を除いた処理部ともいう)に湯を貯留する。 Next, the operation in the cleaning mode in which the waste disposal apparatus 4 cleans the input unit 10 and all the processing units will be described. When a predetermined time elapses after the driving of each of the motors 20G, 70A, 30A, and 40C is stopped, the control unit controls so that hot water is supplied from the second discharge unit 14B of the discharge unit 14. The discharge unit 14 discharges hot water to the charging unit 10 in the cleaning mode. At this time, the control unit drives the motors 20G, 70A, 30A, and 40C to open the first on-off valve 12 and close the second on-off valve 16 of the waste disposal apparatus 4. That is, in the cleaning mode, the waste disposal device 4 discharges hot water from the discharge unit 14 while driving all the processing units. Accordingly, the waste disposal apparatus 4 closes the second on-off valve 16 in the cleaning mode and supplies hot water to the crushing unit 20, the mixer 70, and the dilution tank 30 (hereinafter, also referred to as a processing unit excluding the separation unit 40). To store.
 このとき、制御部は、各モータ20G,70A,30Aを正方向と逆方向とに交互に駆動させる。これによって、貯留された湯が分離部40を除いた処理部内で攪拌されるように流動するため、分離部40を除いた処理部の内面に付着していた破砕物C、攪拌物S、及び希釈物Tに含まれるホットメルトや粘着テープが軟化して粘着力が小さくなり、分離部40を除いた処理部の内面からホットメルトや粘着テープが容易に剥がれる。 At this time, the control unit drives the motors 20G, 70A, 30A alternately in the forward and reverse directions. As a result, the stored hot water flows so as to be stirred in the processing unit excluding the separation unit 40, so that the crushed material C, the agitated material S, and The hot melt and the adhesive tape contained in the diluent T are softened and the adhesive strength is reduced, and the hot melt and the adhesive tape are easily peeled off from the inner surface of the processing section excluding the separation section 40.
 汚物処理装置4は、分離部40を除いた処理部のそれぞれに設けられたヒーターH1、H2、H3を動作させ、分離部40を除いた処理部に貯留した湯を加熱する。これによって、分離部40を除いた処理部の内面に付着するホットメルトや粘着テープをより軟化させて粘着力を小さくし、分離部40を除いた処理部の内面からホットメルトや粘着テープをより良好に剥がすことができる。 The waste disposal apparatus 4 operates the heaters H1, H2, H3 provided in each of the processing units except for the separation unit 40 to heat the hot water stored in the processing units except for the separation unit 40. Thereby, the hot melt or the adhesive tape adhered to the inner surface of the processing unit excluding the separation unit 40 is further softened to reduce the adhesive force, and the hot melt or the adhesive tape is further removed from the inner surface of the processing unit excluding the separation unit 40. Can be peeled off satisfactorily.
 汚物処理装置4は、洗浄モードの際、分離部40を除いた処理部に62℃から65℃の湯を30分以上、及び72℃から87℃の湯を15秒以上のいずれか一方の条件で貯留することによって、分離部40を除いた処理部内の殺菌を行うことができる。 In the cleaning mode, the waste treatment apparatus 4 is configured such that hot water at 62 ° C. to 65 ° C. is supplied for 30 minutes or more, and hot water at 72 ° C. to 87 ° C. is used for 15 seconds or more in the processing unit excluding the separation unit 40. By storing in the processing section, sterilization in the processing section excluding the separation section 40 can be performed.
 次に、汚物処理装置4は、閉じた状態の第2開閉弁16を開いた状態にし、ヒーターH4を動作させる。すると、分離部40を除いた処理部に貯留された湯と共に、分離部40を除いた処理部の内面に付着していたホットメルトや粘着テープを含む破砕物C、攪拌物S、及び希釈物Tが分離部40に流入する。 Next, the waste disposal apparatus 4 opens the second on-off valve 16 in the closed state, and operates the heater H4. Then, together with the hot water stored in the processing unit excluding the separation unit 40, the crushed material C including the hot melt and the adhesive tape adhered to the inner surface of the processing unit excluding the separation unit 40, the agitated material S, and the diluent T flows into the separation unit 40.
 分離部40は、分離部40を除いた処理部の内面に付着していたホットメルトや粘着テープを含む破砕物C、攪拌物S、及び希釈物Tの固形分(分離部40を除いた処理部の内面に付着していたホットメルトや粘着テープを含む)を分離して、分離した固形分を固形分排出部40Dから排出する。 The separation unit 40 includes solids of the crushed material C, the agitated material S, and the diluent T containing the hot melt and the adhesive tape adhered to the inner surface of the processing unit excluding the separation unit 40 (the processing excluding the separation unit 40). (Including hot melt and adhesive tape attached to the inner surface of the solid portion), and the separated solid is discharged from the solid discharge portion 40D.
 このとき、分離部40の内面に付着していた希釈物Tに含まれるホットメルトや粘着テープは、分離部40を除いた処理部に貯留されていた湯が流入することによって軟化して粘着力が小さくなる。これによって、分離部40の内面に付着していたホットメルトや粘着テープを含む希釈物Tの固形分(分離部40の内面に付着していたホットメルトや粘着テープを含む)も、分離部40の内面から剥がれ、固形分排出部40Dから排出される。このとき、62℃から65℃の湯を30分以上、及び72℃から87℃の湯を15秒以上のいずれか一方の条件で連続して分離部40内に湯を流入させることによって、分離部40内に湯が貯留された状態に近い状態にすると、分離部40内の殺菌も行うことができる。 At this time, the hot melt or the adhesive tape contained in the diluent T adhered to the inner surface of the separation unit 40 is softened by the hot water stored in the processing unit excluding the separation unit 40 and the adhesive strength is reduced. Becomes smaller. As a result, the solid content of the diluent T including the hot melt and the adhesive tape adhered to the inner surface of the separation unit 40 (including the hot melt and the adhesive tape adhered to the inner surface of the separation unit 40) is also reduced. And is discharged from the solids discharge section 40D. At this time, the hot water at 62 ° C. to 65 ° C. is continuously fed into the separation unit 40 for at least 30 minutes and the hot water at 72 ° C. to 87 ° C. for 15 seconds or more. By setting the state close to the state where hot water is stored in the section 40, sterilization in the separation section 40 can also be performed.
 このように、第2の汚物処理装置4は、洗浄モードの際、吐出部14から投入部10に湯を吐出することによって、全ての処理部内に残った破砕物C、攪拌物S、及び希釈物Tを洗い流し、全ての処理部を良好な状態にすることができる。 As described above, the second filth disposal apparatus 4 discharges hot water from the discharge unit 14 to the charging unit 10 in the cleaning mode, so that the crushed material C, the stirred material S, and the dilution remaining in all the processing units are discharged. The object T can be washed out and all the processing units can be put in a good state.
 したがって、第2の汚物処理装置4は良好に動作することができる。 Therefore, the second waste disposal apparatus 4 can operate well.
 第2の汚物処理装置4の湯の温度は40℃から90℃である。このため、汚物Dに含まれるホットメルトや粘着テープを軟化させて粘着力を小さくし、全ての処理部の内面からホットメルトや粘着テープを剥がれ易くすると共に、全ての処理部内の殺菌をすることができる。 湯 The temperature of the hot water in the second waste disposal apparatus 4 is 40 ° C to 90 ° C. Therefore, the hot melt or the adhesive tape contained in the waste D is softened to reduce the adhesive strength, the hot melt or the adhesive tape is easily peeled from the inner surface of all the processing units, and the sterilization in all the processing units is performed. Can be.
 第2の汚物処理装置4は全ての処理部の内の下流側の2つの処理部の間に第2開閉弁16を備え、洗浄モードの際に第2開閉弁16を閉じて分離部40を除いた処理部に湯を貯留する。このため、汚物処理装置4は、分離部40を除いた処理部に湯を貯留することによって分離部40を除いた処理部内を良好に洗浄することができる。 The second waste disposal apparatus 4 includes a second on-off valve 16 between two downstream processing units of all the processing units, and closes the second on-off valve 16 in the cleaning mode to disconnect the separation unit 40. Store the hot water in the removed processing unit. For this reason, the waste disposal apparatus 4 can satisfactorily clean the inside of the processing unit excluding the separation unit 40 by storing hot water in the processing unit excluding the separation unit 40.
 第2の汚物処理装置4は、洗浄モードの際、全ての処理部を駆動させつつ、吐出部14から湯を吐出する。このため、汚物処理装置4は、全ての処理部内において湯が攪拌されるように流動することができるため、より良好に全ての処理部内を洗浄することができる。 The second waste disposal apparatus 4 discharges hot water from the discharge unit 14 while driving all the processing units in the cleaning mode. Therefore, the waste disposal apparatus 4 can flow in such a manner that the hot water is stirred in all the processing sections, so that the inside of all the processing sections can be more appropriately cleaned.
 第2の汚物処理装置4は、全ての処理部に設けられ、全ての処理部内の水及び湯の少なくともいずれか一方を加熱するヒーターH1,H2,H3,H4を備えている。このため、全ての処理部において、ヒーターH1,H2,H3,H4によって加熱された水及び湯の少なくともいずれか一方によって、破砕物C、攪拌物S、及び希釈物Tに含まれるホットメルトや粘着テープを軟化させて粘着力を小さくし、全ての処理部の内面からホットメルトや粘着テープを剥がれ易くすると共に、全ての処理部内の殺菌をすることができる。 The second waste disposal apparatus 4 includes heaters H1, H2, H3, and H4 that are provided in all processing units and heat at least one of water and hot water in all processing units. For this reason, in all the processing units, hot melt or adhesive contained in the crushed material C, the agitated material S, and the dilute material T is generated by at least one of water and hot water heated by the heaters H1, H2, H3, and H4. The tape can be softened to reduce the adhesive strength, the hot melt or the adhesive tape can be easily peeled off from the inner surface of all the processing sections, and the sterilization in all the processing sections can be performed.
<実施形態5>
 第3の汚物処理装置の実施形態5の汚物処理装置5は、汚物である使用済の紙おむつや生理用品やペット用の砂等を破砕して、下水管に排出する装置である。これら汚物は、パルプ、プラスティック、及び高吸水性ポリマー(SAP,super absorbent polymer、以下単にポリマーと表記する)等で形成されている。これら紙おむつや生理用品やペット用の砂は使用されるとパルプやポリマーが水分を吸収保持する。水分が吸収保持されたポリマーに分解剤であるCaCl2(塩化カルシウム)等を反応させると、ポリマーから水分を取り出すことができる。分解剤としてCaCl2を反応させたポリマーは再び水分を吸収保持することができない不可逆状態になる。
<Embodiment 5>
The waste disposal apparatus 5 of Embodiment 3 of the third waste disposal apparatus is an apparatus for crushing used paper diapers, sanitary products, pet sand, and the like, which are waste, and discharging the waste to a sewer pipe. These wastes are formed of pulp, plastic, superabsorbent polymer (SAP, superabsorbent polymer, hereinafter simply referred to as polymer), and the like. When these disposable diapers, sanitary products, and pet sand are used, the pulp and polymer absorb and retain moisture. By reacting CaCl 2 (calcium chloride) or the like as a decomposing agent with the polymer having absorbed and retained the water, the water can be extracted from the polymer. The polymer reacted with CaCl 2 as a decomposing agent is again in an irreversible state where it cannot absorb and retain moisture.
 第3の汚物処理装置5は、図5に示すように、使用済みの紙おむつや生理用品やペット用の砂(以降、汚物Dともいう)を投入する投入口が形成された投入部10、破砕部20、シュート21、ミキサ70、排出路11、第1開閉弁12、希釈槽30、分解剤投入装置13、脱臭装置80、吐出部14、排水路15、第2開閉弁16、分離部40、第1通気路17、負圧解消部17A、第2通気路18、及び第3通気路19を備えている。 As shown in FIG. 5, the third waste disposal apparatus 5 includes an input unit 10 having an input port for inputting used paper diapers, sanitary products, and sand for pets (hereinafter, also referred to as waste D). Part 20, chute 21, mixer 70, discharge path 11, first opening / closing valve 12, dilution tank 30, decomposing agent introducing device 13, deodorizing device 80, discharging section 14, drainage path 15, second opening / closing valve 16, separation section 40 , A first ventilation path 17, a negative pressure eliminating section 17A, a second ventilation path 18, and a third ventilation path 19.
 投入部10、破砕部20、シュート21、ミキサ70、希釈槽30、分離部40、及びトラップ15Aのそれぞれは、水分を吸収保持可能なポリマーを有する汚物Dを分離処理し、直列に接続された複数の処理部である。 Each of the charging unit 10, the crushing unit 20, the chute 21, the mixer 70, the dilution tank 30, the separating unit 40, and the trap 15A separates the waste D having a polymer capable of absorbing and holding moisture, and is connected in series. There are a plurality of processing units.
 これら処理部は、下流側の処理部が一回の処理で処理できる処理量が上流側の処理部が一回の処理で処理できる処理量以上である。具体的には、破砕部20が一回の処理で処理できる処理量は投入部10が一回の処理で処理できる処理量以上である。シュート21が一回の処理で処理できる処理量は破砕部20が一回の処理で処理できる処理量以上である。ミキサ70が一回の処理で処理できる処理量はシュート21が一回の処理で処理できる処理量以上である。希釈槽30が一回の処理で処理できる処理量はミキサ70が一回の処理で処理できる処理量以上である。分離部40が一回の処理で処理できる処理量は希釈槽30が一回の処理で処理できる処理量以上である。 With these processing units, the processing amount that the downstream processing unit can process in one process is equal to or larger than the processing amount that the upstream processing unit can process in one process. Specifically, the processing amount that can be processed by the crushing unit 20 in one process is equal to or larger than the processing amount that can be processed by the input unit 10 in one process. The processing amount that can be processed by the chute 21 in one processing is equal to or larger than the processing amount that can be processed by the crushing unit 20 in one processing. The processing amount that can be processed by the mixer 70 in one process is equal to or larger than the processing amount that the chute 21 can process in one process. The processing amount that the dilution tank 30 can process in one process is equal to or larger than the processing amount that the mixer 70 can process in one process. The processing amount that can be processed by the separation unit 40 in one process is equal to or larger than the processing amount that the dilution tank 30 can process in one process.
 汚物処理装置5は複数の処理部で構成された第1グループG1、第2グループG2、及び第3グループG3を備えている。第1グループG1は投入部10、破砕部20、シュート21、及びミキサ70で構成されている。第2グループG2は希釈槽30で構成されている。第3グループG3は分離部40、及びトラップ15Aで構成されている。汚物処理装置5は1つ及び複数の少なくともいずれか一方の処理部で複数のグループを構成している。 The waste disposal apparatus 5 includes a first group G1, a second group G2, and a third group G3 each including a plurality of processing units. The first group G <b> 1 includes a charging unit 10, a crushing unit 20, a chute 21, and a mixer 70. The second group G2 includes a dilution tank 30. The third group G3 includes the separation unit 40 and the trap 15A. The waste disposal apparatus 5 forms a plurality of groups by one and / or a plurality of at least one treatment unit.
 投入部10は、上下方向に延び、筒状をなし上端に開口して投入口が形成されている。投入口には投入口を開閉する第1蓋60が設けられている。投入部10には、水分を吸収保持可能なポリマーを有する所定の量の汚物Dを投入する。投入部10に所定の量の汚物Dを投入すると、所定の量の汚物Dはおよそ5秒間で投入部10を通過し、後述する破砕部20に投入される。所定の量の汚物Dの量は、投入部10で一回の処理で処理できる量である。 (4) The charging section 10 extends in the up-down direction, has a cylindrical shape, and is opened at an upper end to form a charging port. The input port is provided with a first lid 60 for opening and closing the input port. A predetermined amount of filth D having a polymer capable of absorbing and retaining moisture is charged into the charging section 10. When a predetermined amount of filth D is input into the input unit 10, the predetermined amount of filth D passes through the input unit 10 for about 5 seconds and is input into the crushing unit 20 described later. The predetermined amount of the waste D is an amount that can be processed in the input unit 10 in one process.
 破砕部20は、破砕機(例えば、公知のディスポーザーやシュレッダー)が用いられる。破砕部20の上端は投入部10の下端に連結されている。破砕部20の側面には、破砕部20を駆動するモータ20Gが破砕部20に対して着脱自在に取り付けられている。モータ20Gは制御部(図示せず)によって動作が制御される。破砕部20は投入部10に投入された所定の量の汚物Dをおよそ20秒間で破砕して所定の量の汚物Dを含む破砕物C(以降、破砕物Cともいう)にする。 は The crushing unit 20 uses a crusher (for example, a known disposer or shredder). The upper end of the crushing section 20 is connected to the lower end of the charging section 10. A motor 20G for driving the crushing unit 20 is detachably attached to the side surface of the crushing unit 20 with respect to the crushing unit 20. The operation of the motor 20G is controlled by a control unit (not shown). The crushing unit 20 crushes a predetermined amount of the filth D charged into the input unit 10 in about 20 seconds to form a crushed material C including a predetermined amount of the filth D (hereinafter, also referred to as a crushed material C).
 制御部は、例えば、マイクロコンピュータを含んだ制御回路として構成され、CPUや記憶部等を有している。制御部には操作部(図示せず)が電気的に接続されており、汚物処理装置5を使用する使用者が操作部を操作することによって、汚物処理装置5の動作を開始したり終了したりし得る構成となっている。 The control unit is configured as a control circuit including a microcomputer, for example, and has a CPU, a storage unit, and the like. An operation unit (not shown) is electrically connected to the control unit, and the user of the waste disposal apparatus 5 operates the operation unit to start or end the operation of the waste disposal apparatus 5. It has a configuration that can be used.
 破砕部20のモータ20Gには、制御部が電気的に接続されている。制御部は破砕部20のモータ20Gが消費する消費電力量の大きさを検出して、検出した消費電力量の大きさに基づいて破砕部20に係る第1負荷を検出し得る構成とされている。具体的には、破砕部20のモータ20Gが消費する消費電力量の大きさと第1負荷の大きさとは正比例しているものとして捉え、消費電力量の大きさが紙おむつの大きさに比例しているものとする。 制 御 A control unit is electrically connected to the motor 20G of the crushing unit 20. The control unit is configured to detect the amount of power consumption consumed by the motor 20G of the crushing unit 20 and detect the first load related to the crushing unit 20 based on the detected amount of power consumption. I have. Specifically, the magnitude of the power consumption consumed by the motor 20G of the crushing unit 20 and the magnitude of the first load are regarded as being directly proportional, and the magnitude of the power consumption is proportional to the size of the disposable diaper. Shall be
 シュート21は上端から下端に向けて縮径して形成された筒状をなしており、上端が破砕部20の下端に連結されている。シュート21は破砕部20から破砕物Cを後述するミキサ70に案内する。破砕物Cはおよそ5秒間でシュート21を通過してミキサ70に投入される。シュート21の下端には第2蓋22が設けられている。第2蓋22は、例えば、フラッパー弁等が用いられる。第2蓋22は、破砕物C等が載置されない状態ではシュート21の下端を閉鎖する。第2蓋22は、破砕物C等が載置されると、破砕物C等の重さによって垂下してシュート21の下端を解放する。第2蓋22は、載置された破砕物C等がミキサ70に流入すると、再びシュート21の下端を閉鎖する。第2蓋22はミキサ70から破砕部20や投入部10に向けて後述する攪拌物Sが飛散したり、臭気が立ち昇ったりすることを抑えることができる。 The chute 21 has a cylindrical shape formed by reducing the diameter from the upper end to the lower end, and the upper end is connected to the lower end of the crushing unit 20. The chute 21 guides the crushed material C from the crushing unit 20 to a mixer 70 described later. The crushed material C passes through the chute 21 for about 5 seconds and is charged into the mixer 70. A second lid 22 is provided at a lower end of the chute 21. As the second lid 22, for example, a flapper valve or the like is used. The second lid 22 closes the lower end of the chute 21 when the crushed material C or the like is not placed. When the crushed material C or the like is placed, the second lid 22 hangs down by the weight of the crushed material C or the like and releases the lower end of the chute 21. The second lid 22 closes the lower end of the chute 21 again when the placed crushed material C or the like flows into the mixer 70. The second lid 22 can prevent the later-described agitated material S from being scattered from the mixer 70 toward the crushing unit 20 and the charging unit 10 and prevent the odor from rising and rising.
 ミキサ70は上端がシュート21の下端に連結されている。ミキサ70の下面には、ミキサ70を駆動するモータ70Aがミキサ70に対して着脱自在に取り付けられている。ミキサ70は破砕物Cと分解剤とをおよそ60秒間で攪拌して所定の量の汚物Dを含む攪拌物S(以降、攪拌物Sともいう)にする。ミキサ70のモータ70Aには、制御部が電気的に接続されている。制御部はミキサ70のモータ70Aが消費する消費電流の大きさを検出して、検出した消費電流の大きさに基づいてミキサ70に係る第2負荷を検出し得る構成とされている。具体的には、ミキサ70のモータ70Aが消費する消費電流の大きさが稼働中に所定値を上回るときに、後述するポリマーの反応が完了していないものとする。制御部は第1グループG1(投入部10、破砕部20、シュート21、及びミキサ70)内に攪拌物Sのみが有るか否か、及び第1グループG1内が空の状態であるか否かを判別し得る構成とされている。 The mixer 70 has its upper end connected to the lower end of the chute 21. On the lower surface of the mixer 70, a motor 70A for driving the mixer 70 is detachably attached to the mixer 70. The mixer 70 agitates the crushed material C and the decomposing agent for about 60 seconds to form a stirred material S (hereinafter, also referred to as a stirred material S) containing a predetermined amount of filth D. The control unit is electrically connected to the motor 70A of the mixer 70. The control unit is configured to detect the magnitude of the current consumed by the motor 70A of the mixer 70 and to detect the second load related to the mixer 70 based on the detected magnitude of the consumed current. Specifically, when the magnitude of the current consumed by the motor 70A of the mixer 70 exceeds a predetermined value during operation, it is assumed that the polymer reaction described below has not been completed. The control unit determines whether there is only the agitated material S in the first group G1 (the charging unit 10, the crushing unit 20, the chute 21, and the mixer 70), and whether the first group G1 is empty. Is determined.
 排出路11は一端がミキサ70に連通している。排出路11の他端は後述する希釈槽30に連通している。第1開閉弁12は、例えば、公知の電動ボールバルブである。第1開閉弁12は排出路11に設けられ、排出路11を開閉する。第1開閉弁12は制御部によって開閉する動作が制御される。 One end of the discharge path 11 communicates with the mixer 70. The other end of the discharge path 11 communicates with a dilution tank 30 described later. The first on-off valve 12 is, for example, a known electric ball valve. The first on-off valve 12 is provided in the discharge path 11 and opens and closes the discharge path 11. The operation of opening and closing the first on-off valve 12 is controlled by the control unit.
 第1開閉弁12の上流側の排出路11には手動で開閉する第1手動開閉弁12Aが設けられている。第1手動開閉弁12Aは常時開いた状態にされており、第1グループG1及び第2グループG2のいずれか一方を汚物処理装置5から取り外す場合に閉じた状態にする。第1手動開閉弁12Aと第1開閉弁12との間の排出路11には、排出路11を第1手動開閉弁12A側と第1開閉弁12側とに自在に切り離しし得る構成とされた第1接続部11Aが設けられている。 排出 A first manual opening / closing valve 12 </ b> A that is manually opened / closed is provided in the discharge path 11 on the upstream side of the first opening / closing valve 12. The first manual on-off valve 12A is always open, and is closed when any one of the first group G1 and the second group G2 is removed from the waste disposal apparatus 5. The discharge path 11 between the first manual open / close valve 12A and the first open / close valve 12 is configured so that the discharge path 11 can be freely separated into the first manual open / close valve 12A side and the first open / close valve 12 side. A first connection portion 11A is provided.
 第1接続部11Aは、例えば、第1手動開閉弁12A側と第1開閉弁12側とのそれぞれの排出路11の端に鍔部が形成され、これら鍔部の端面同士が当接されている。第1接続部11Aは、これら鍔部の端面同士を当接した状態に保持する保持部材によって連通した状態にされている(図示せず。)。第1接続部11Aは、近傍に第1手動開閉弁12Aと第1開閉弁12とが設けられ、第1グループG1、及び第2グループG2同士を接続する。 In the first connection portion 11A, for example, a flange portion is formed at the end of each of the discharge passages 11 on the first manual on-off valve 12A side and the first on-off valve 12 side, and the end surfaces of these flange portions are brought into contact with each other. I have. The first connecting portion 11A is in communication with a holding member that holds the end surfaces of the flange portions in contact with each other (not shown). The first connection portion 11A is provided with a first manual on-off valve 12A and a first on-off valve 12 in the vicinity, and connects the first group G1 and the second group G2.
 希釈槽30は攪拌物Sを後述する吐出部14から供給された水及び湯の少なくともいずれか一方で希釈しておよそ85秒間で所定の量の汚物Dを含む希釈物T(以降、希釈物Tともいう)にする。希釈槽30の上面には排出路11の他端が連結されており、排出路11が希釈槽30内に連通している。希釈槽30は破砕部20の下流側に連通している。希釈槽30の上面にはモータ30Aが希釈槽30に対して着脱自在に取り付けられている。希釈槽30内にはモータ30Aの回転軸に対して着脱自在に連結されたプロペラ(図示せず)が配置されている。 The diluting tank 30 dilutes the agitated material S with at least one of water and hot water supplied from a discharge unit 14 described later and dilutes T containing a predetermined amount of filth D in about 85 seconds (hereinafter, diluent T Also called). The other end of the discharge path 11 is connected to the upper surface of the dilution tank 30, and the discharge path 11 communicates with the inside of the dilution tank 30. The dilution tank 30 communicates with the downstream side of the crushing section 20. On the upper surface of the dilution tank 30, a motor 30A is detachably attached to the dilution tank 30. A propeller (not shown) is detachably connected to the rotation shaft of the motor 30A in the dilution tank 30.
 プロペラはモータ30Aが取り外された場合でも、希釈槽30内における姿勢が変化しないようにされている。モータ30Aは希釈槽30及びプロペラに対して着脱自在である。希釈槽30のモータ30Aは制御部によって動作が制御される。制御部は第2グループG2(希釈槽30)内が空の状態であるか否かを判別し得る構成とされている。 The propeller does not change its posture in the dilution tank 30 even when the motor 30A is removed. The motor 30A is detachable from the dilution tank 30 and the propeller. The operation of the motor 30A of the dilution tank 30 is controlled by the control unit. The control unit is configured to be able to determine whether or not the second group G2 (dilution tank 30) is empty.
 希釈槽30の側面には点検口30Bが形成されている。点検口30Bは蓋30Cによって水密状に閉鎖されている。希釈槽30内を点検する際には、蓋30Cを外し、点検口30Bから希釈槽30内を点検する。制御部は点検口30Bが蓋30Cによって閉鎖されている状態か閉鎖されていない状態かを判別し得る構成とされている。制御部は、点検口30Bが蓋30Cによって閉鎖されていない状態であると判別すると、汚物処理装置5を動作させないように制御する。 点 検 An inspection port 30B is formed on the side surface of the dilution tank 30. The inspection port 30B is closed in a watertight manner by a lid 30C. When inspecting the inside of the dilution tank 30, the lid 30C is removed, and the inside of the dilution tank 30 is inspected from the inspection port 30B. The control unit is configured to be able to determine whether the inspection port 30B is closed or not closed by the lid 30C. When the control unit determines that the inspection port 30B is not closed by the lid 30C, the control unit controls the waste disposal apparatus 5 not to operate.
 希釈槽30のモータ30Aには、制御部が電気的に接続されている。制御部は希釈槽30のモータ30Aが消費する消費電流の大きさを検出して、検出した消費電流の大きさに基づいて希釈槽30に係る第3負荷を検出し得る構成とされている。具体的には、希釈槽30のモータ30Aが消費する消費電流の大きさが所定値を超える時に後述するポリマーの反応が完了していないものとする。 制 御 A control unit is electrically connected to the motor 30A of the dilution tank 30. The control unit is configured to detect the magnitude of the current consumed by the motor 30A of the dilution tank 30, and to detect the third load related to the dilution tank 30 based on the detected magnitude of the consumed current. Specifically, it is assumed that when the magnitude of the current consumed by the motor 30A of the dilution tank 30 exceeds a predetermined value, the reaction of the polymer described later has not been completed.
 分解剤投入装置13は分解剤をシュート21内に投入する。分解剤投入装置13は、シュート21の側面に取り付けられている。分解剤投入装置13は、例えば、公知のフィーダー等が用いられ、制御部によってシュート21に所定の量の分解剤を投入するように制御される。所定の量の分解剤の量は、所定の量の汚物Dに含まれるポリマーから水分を満遍なく取り出すことができる量である。 The decomposing agent input device 13 inputs the decomposing agent into the chute 21. The decomposing agent introducing device 13 is attached to a side surface of the chute 21. For example, a known feeder or the like is used as the decomposing agent introducing device 13, and the control unit controls the chute 21 to supply a predetermined amount of the decomposing agent. The amount of the predetermined amount of the decomposing agent is an amount capable of uniformly extracting water from the polymer contained in the predetermined amount of the waste D.
 分解剤投入装置13は、制御部が電気的に接続されている。制御部は、第1負荷の大きさに対応する信号、第2負荷の大きさに対応する信号、及び第3負荷の大きさに対応する信号に基づいて分解剤を分解剤投入装置13から投入するように分解剤投入装置13を制御する。 制 御 The control unit of the decomposing agent charging device 13 is electrically connected. The control unit supplies the decomposing agent from the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, the signal corresponding to the magnitude of the second load, and the signal corresponding to the magnitude of the third load. The decomposing agent feeding device 13 is controlled so as to perform the above.
 脱臭装置80は、吸気部80A、脱臭部80B、及び送風部80Cを有している。吸気部80Aには、例えば、公知の軸流ファン等が用いられる。吸気部80Aは、一端面から吸気し、他端面から送風する。吸気部80Aは制御部に電気的に接続されている。吸気部80Aは投入部10の側面に形成された第1接続口10Dを一端面で覆うように取り付けられている。吸気部80Aは投入部10から吸気する。脱臭部80Bには、例えば、活性炭が付着した不織布等で形成された、所謂、脱臭フィルターが用いられる。脱臭部80Bは、吸気部80Aの他端面(すなわち、送風する面)を覆うように配置される。 The deodorizing device 80 has an intake unit 80A, a deodorizing unit 80B, and a blowing unit 80C. For example, a known axial fan or the like is used for the intake section 80A. The suction section 80A sucks in air from one end face and blows air from the other end face. The suction unit 80A is electrically connected to the control unit. The suction unit 80A is attached so as to cover the first connection port 10D formed on the side surface of the insertion unit 10 with one end surface. The intake section 80A takes in air from the input section 10. For the deodorizing section 80B, for example, a so-called deodorizing filter formed of a nonwoven fabric or the like to which activated carbon is attached is used. The deodorizing section 80B is arranged so as to cover the other end face (that is, the air blowing face) of the suction section 80A.
 送風部80Cは吸気部80Aと同様の構成であり、例えば、公知の軸流ファン等が用いられる。送風部80Cは制御部に電気的に接続されている。送風部80Cは投入部10の側面に形成された第2接続口10Eを他端面で覆うように取り付けられている。投入部10は脱臭装置80を介して大気解放されている。送風部80Cは投入部10に送風する。脱臭装置80は汚物D及び破砕物Cの少なくともいずれか一方から生じる臭気を脱臭する。脱臭装置80は第1接続口10D及び第2接続口10Eに接続されている。 風 The blower unit 80C has the same configuration as the suction unit 80A, and for example, a known axial fan or the like is used. The blowing unit 80C is electrically connected to the control unit. The blowing unit 80C is attached so as to cover the second connection port 10E formed on the side surface of the charging unit 10 with the other end surface. The charging section 10 is open to the atmosphere via a deodorizing device 80. The blowing unit 80C blows air to the charging unit 10. The deodorizing device 80 deodorizes the odor generated from at least one of the waste D and the crushed material C. The deodorizing device 80 is connected to the first connection port 10D and the second connection port 10E.
 吐出部14は破砕部20に水及び湯の少なくともいずれか一方を供給する。吐出部14は水を供給する第1吐出部14A、及び湯を供給する第2吐出部14Bを有している。吐出部14は投入部10に設けられている。第1吐出部14A、第2吐出部14Bのそれぞれには第1電磁弁14C、第2電磁弁14Dが設けられている。 The discharge unit 14 supplies at least one of water and hot water to the crushing unit 20. The discharge unit 14 has a first discharge unit 14A that supplies water and a second discharge unit 14B that supplies hot water. The discharge unit 14 is provided in the input unit 10. A first solenoid valve 14C and a second solenoid valve 14D are provided in each of the first ejection section 14A and the second ejection section 14B.
 これら第1電磁弁14C、及び第2電磁弁14Dは制御部によって所定の条件に基づいて破砕部20に水や湯を供給するように制御される。具体的には、制御部は、破砕部20のモータ20Gの駆動が停止してからの経過時間をカウントしたり、破砕部20のモータ20Gが駆動された回数をカウントしたり、分解剤が投入された量や分解剤が投入された回数をカウントしたり、所定の時間をカウントしたりし得る構成とされている。これによって、制御部は破砕部20が動作を停止した後の所定の経過時間、破砕部20が動作した所定の回数毎、分解剤の所定の投入量毎及び所定の投入回数毎の少なくともいずれか一方、及び所定の時間毎のいずれかに、吐出部14が水及び湯の少なくともいずれか一方を供給するように制御する。これによって、破砕部20、ミキサ70、希釈槽30、分離部40を洗浄することができる。 The first solenoid valve 14C and the second solenoid valve 14D are controlled by the control unit to supply water or hot water to the crushing unit 20 based on predetermined conditions. Specifically, the control unit counts the elapsed time since the driving of the motor 20G of the crushing unit 20 is stopped, counts the number of times the motor 20G of the crushing unit 20 is driven, and inputs the disintegrant. It is configured to be able to count the amount of the disintegration agent or the number of times the disintegrant has been charged or to count a predetermined time. Thereby, the control unit determines at least one of a predetermined elapsed time after the operation of the crushing unit 20 has stopped, a predetermined number of times the crushing unit 20 has operated, a predetermined amount of the disintegrant, and a predetermined number of times of the injection. On the other hand, the discharge unit 14 is controlled so as to supply at least one of water and hot water at any one of the predetermined times. Thereby, the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 can be washed.
 排水路15は一端が希釈槽30の下端に連通して連結されている。排水路15の他端は下水管(図示せず)に連通している。排水路15にはトラップ15Aが形成されている。トラップ15Aにはゼット排水部が接続されている(図示せず。)。排水路15は希釈物Tの水分をおよそ5秒間で下水管に向けて流すことができる。第2開閉弁16は、例えば、公知の電動ボールバルブである。第2開閉弁16は排水路15のトラップ15Aよりも上流側に設けられ、排水路15を開閉する。第2開閉弁16は制御部によって開閉する動作が制御される。 The drainage channel 15 is connected at one end to the lower end of the dilution tank 30. The other end of the drain 15 communicates with a sewer pipe (not shown). A trap 15 </ b> A is formed in the drainage channel 15. A jet drain section is connected to the trap 15A (not shown). The drain 15 allows the water of the diluent T to flow toward the drain in about 5 seconds. The second on-off valve 16 is, for example, a known electric ball valve. The second on-off valve 16 is provided upstream of the trap 15 </ b> A of the drainage channel 15 and opens and closes the drainage channel 15. The operation of opening and closing the second on-off valve 16 is controlled by the control unit.
 第2開閉弁16の上流側の排水路15には手動で開閉する第2手動開閉弁16Aが設けられている。第2手動開閉弁16Aは常時開いた状態にされており、第2グループG2及び第3グループG3のいずれか一方を汚物処理装置5から取り外す場合に閉じた状態にする。第2手動開閉弁16Aと第2開閉弁16との間の排水路15には、排水路15を第2手動開閉弁16A側と第2開閉弁16側とに自在に切り離しし得る構成とされた第2接続部15Bが設けられている。 排水 A second manual opening / closing valve 16 </ b> A that is manually opened / closed is provided in the drainage channel 15 on the upstream side of the second opening / closing valve 16. The second manual on-off valve 16A is always open, and is closed when one of the second group G2 and the third group G3 is removed from the waste disposal apparatus 5. The drainage channel 15 between the second manual on-off valve 16A and the second on-off valve 16 is configured so that the drainage channel 15 can be freely separated into the second manual on-off valve 16A side and the second on-off valve 16 side. A second connection portion 15B is provided.
 第2接続部15Bは、例えば、第2手動開閉弁16A側と第2開閉弁16側とのそれぞれの排水路15の端に鍔部が形成され、これら鍔部の端面同士が当接されている。第2接続部15Bは、これら鍔部の端面同士を当接した状態に保持する保持部材によって連通した状態にされている(図示せず。)。第2接続部15Bは、近傍に第2手動開閉弁16Aと第2開閉弁16とが設けられ、第2グループG2、及び第3グループG3同士を接続する。 In the second connection portion 15B, for example, a flange portion is formed at an end of each of the drainage channels 15 on the second manual on-off valve 16A side and the second on-off valve 16 side, and end surfaces of these flange portions are brought into contact with each other. I have. The second connection portion 15B is in communication with a holding member that holds the end surfaces of the flange portions in contact with each other (not shown). The second connection portion 15B is provided with a second manual on-off valve 16A and a second on-off valve 16 in the vicinity, and connects the second group G2 and the third group G3.
 分離部40はトラップ15Aと第2開閉弁16との間の排水路15に設けられている。分離部40は希釈槽30の下流側に接続されている。分離部40は、例えば、公知のスクリュープレス装置等が用いられる。分離部40の側面には、分離部40を駆動するモータ40Cが分離部40に対して着脱自在に取り付けられている。分離部40の上端部には希釈物Tから分離した固形分を排出する固形分排出部40Dが連結している。分離部40はおよそ75秒間で排水路15を流れる希釈物Tから固形分を分離して取り出すことができる。分離部40のモータ40Cは制御部によって動作が制御される。 The separation unit 40 is provided in the drainage channel 15 between the trap 15A and the second on-off valve 16. The separation section 40 is connected to the downstream side of the dilution tank 30. As the separation unit 40, for example, a known screw press device or the like is used. A motor 40C for driving the separating unit 40 is detachably attached to the side of the separating unit 40 with respect to the separating unit 40. A solids discharge section 40D for discharging solids separated from the diluent T is connected to the upper end of the separation section 40. The separation unit 40 can separate and extract solids from the diluent T flowing through the drainage channel 15 in about 75 seconds. The operation of the motor 40C of the separation unit 40 is controlled by the control unit.
 制御部は第3グループG3(分離部40)内が空の状態であるか否かを判別し得る構成とされている。 The control unit is configured to be able to determine whether or not the third group G3 (separation unit 40) is empty.
 分離部40の側面には点検口40Aが形成されている。点検口40Aは蓋40Bによって水密状に閉鎖されている。分離部40内を点検する際には、蓋40Bを外し、点検口40Aから分離部40内を点検する。制御部は、点検口40Aが蓋40Bによって閉鎖されていない状態であると判別すると、汚物処理装置5を動作させないように制御する。 点 検 An inspection port 40A is formed on the side surface of the separation unit 40. The inspection port 40A is closed in a watertight manner by a lid 40B. When inspecting the inside of the separation unit 40, the lid 40B is removed, and the inside of the separation unit 40 is inspected from the inspection port 40A. When the control unit determines that the inspection port 40A is not closed by the lid 40B, the control unit controls the waste disposal apparatus 5 not to operate.
 第1通気路17は、一端が第1接続口10D及び第2接続口10Eよりも下流側の投入部10に連通し、他端が希釈槽30の上端に接続され、希釈槽30内に連通している。第1通気路17の一端は投入部10に対して着脱自在であり、他端は希釈槽30に対して着脱自在である。負圧解消部17Aは第1通気路17に取り付けられている。負圧解消部17Aには、例えば、公知のドルゴ通気弁やコバート通気弁等が用いられる。 One end of the first ventilation path 17 communicates with the charging section 10 downstream of the first connection port 10D and the second connection port 10E, and the other end is connected to the upper end of the dilution tank 30 and communicates with the dilution tank 30. doing. One end of the first ventilation path 17 is detachable from the charging section 10, and the other end is detachable from the dilution tank 30. The negative pressure eliminating section 17A is attached to the first ventilation path 17. For the negative pressure eliminating section 17A, for example, a well-known Dolgo ventilation valve, a covert ventilation valve, or the like is used.
 第2通気路18は、一端が第1通気路17の負圧解消部17Aの下流側に連通して接続され、他端が分離部40の上端に連通して接続され、分離部40内に連通している。第2通気路18の他端は分離部40に対して着脱自在である。負圧解消部17Aは、第1通気路17及び第2通気路18を介して、希釈槽30内及び分離部40内の負圧を解消する。 One end of the second ventilation path 18 is connected to and connected to the downstream side of the negative pressure eliminating section 17A of the first ventilation path 17, and the other end is connected to and connected to the upper end of the separation section 40. Communicating. The other end of the second ventilation path 18 is detachable from the separation section 40. The negative pressure eliminating section 17A eliminates the negative pressure in the dilution tank 30 and the separation section 40 via the first ventilation path 17 and the second ventilation path 18.
 第3通気路19は、一端が投入部10の側面に連通して接続され、他端が分離部40の固形分排出部40Dに連通して接続されている。第3通気路19の一端は投入部10に対して着脱自在であり、他端は固形分排出部40Dに対して着脱自在である。第3通気路19には、吸気部19Aが取り付けられている。吸気部19Aは、脱臭装置80の送風部80C、及び吸気部80Aと同様の構成であり、例えば、公知の軸流ファン等が用いられる。吸気部19Aは制御部に電気的に接続されている。吸気部19Aは、吸気部19Aを駆動した際に、第3通気路19内の空気が固形分排出部40Dから投入部10に向けて流れるように第3通気路19に取り付けられている。 The third ventilation path 19 has one end connected to and connected to the side surface of the charging section 10, and the other end connected to and connected to the solids discharge section 40 </ b> D of the separation section 40. One end of the third ventilation path 19 is detachable from the charging section 10 and the other end is detachable from the solids discharge section 40D. An intake unit 19A is attached to the third ventilation path 19. The suction unit 19A has the same configuration as the blowing unit 80C and the suction unit 80A of the deodorizing device 80, and for example, a known axial fan or the like is used. The suction unit 19A is electrically connected to the control unit. The suction section 19A is attached to the third ventilation path 19 so that when the suction section 19A is driven, the air in the third ventilation path 19 flows from the solids discharge section 40D toward the charging section 10.
 第1グループG1(投入部10、破砕部20、シュート21、及びミキサ70)における処理時間の合計は、5秒間(投入部10)+20秒間(破砕部20)+5秒間(シュート21)+60秒間(ミキサ70)=90秒間である。第2グループG2(希釈槽30)における処理時間の合計は、85秒間(希釈槽30)=85秒間である。第3グループG3は(分離部40、及びトラップ15A)における処理時間の合計は、75秒間(分離部40)+5秒間(トラップ15A)=80秒間である。第1グループG1、第2グループG2、及び第3グループG3のそれぞれの処理時間はほぼ等しい。詳しくは、第1グループG1、第2グループG2、及び第3グループG3のそれぞれの処理時間は下流側のグループになるほど短くなる。つまり、上流側のグループよりも下流側のグループの処理時間が短い。 The total processing time in the first group G1 (the charging unit 10, the crushing unit 20, the chute 21, and the mixer 70) is 5 seconds (the charging unit 10) +20 seconds (the crushing unit 20) +5 seconds (the chute 21) +60 seconds ( Mixer 70) = 90 seconds. The total processing time in the second group G2 (dilution tank 30) is 85 seconds (dilution tank 30) = 85 seconds. In the third group G3, the total processing time in the (separator 40 and the trap 15A) is 75 seconds (separator 40) +5 seconds (trap 15A) = 80 seconds. The processing times of the first group G1, the second group G2, and the third group G3 are substantially equal. Specifically, the processing time of each of the first group G1, the second group G2, and the third group G3 becomes shorter as the group is located on the downstream side. That is, the processing time of the group on the downstream side is shorter than that of the group on the upstream side.
 第1グループG1、第2グループG2、及び第3グループG3のそれぞれは、汚物処理装置5から取り外し得る構成とされている。詳しくは、第1グループG1を汚物処理装置5から取り外す場合、モータ20G、及びモータ70Aは汚物処理装置5内に置き残される。第2グループG2を汚物処理装置5から取り外す場合には、モータ30Aが汚物処理装置5内に置き残される。第3グループG3を汚物処理装置5から取り外す場合、モータ40Cは汚物処理装置5内に置き残される。第1通気路17、第2通気路18、及び第3通気路19は、各グループのいずれを取り外す場合においても汚物処理装置5内に置き残される。 1Each of the first group G1, the second group G2, and the third group G3 is configured to be removable from the waste disposal apparatus 5. Specifically, when removing the first group G1 from the waste disposal apparatus 5, the motor 20G and the motor 70A are left inside the waste disposal apparatus 5. When removing the second group G2 from the waste disposal apparatus 5, the motor 30A is left inside the waste disposal apparatus 5. When removing the third group G3 from the waste disposal apparatus 5, the motor 40C is left inside the waste disposal apparatus 5. The first ventilation path 17, the second ventilation path 18, and the third ventilation path 19 are left in the waste disposal apparatus 5 when any of the groups is removed.
 次に、第3の汚物処理装置5の動作について説明する。先ず、第1蓋60を起立状態にして投入口を解放し、所定の量の汚物Dを投入部10に投入する。第1蓋60を起立状態にしたことに基づいて、制御部によって脱臭装置80の吸気部80A、及び送風部80Cの動作が開始される。次に、第1蓋60を倒伏状態にして投入部10の投入口を閉鎖し、操作部(図示せず)を操作して汚物処理装置5を動作させる。 Next, the operation of the third waste disposal apparatus 5 will be described. First, the first lid 60 is placed in an upright state, the inlet is opened, and a predetermined amount of waste D is injected into the inlet 10. Based on the fact that the first lid 60 is in the upright state, the control unit starts the operation of the suction unit 80A and the blower unit 80C of the deodorization device 80. Next, the first lid 60 is placed in the lying state, the slot of the slot 10 is closed, and the operation unit (not shown) is operated to operate the waste disposal apparatus 5.
 汚物処理装置5は、先ず、制御部によって第1電磁弁14C及び第2電磁弁14Dの少なくともいずれか一方を動作させて、吐出部14から第1所定量の水及び湯の少なくともいずれか一方を破砕部20に供給する。こうして、破砕部20に所定の量の汚物Dと水及び湯の少なくともいずれか一方とが投入される。このとき、第1手動開閉弁12Aは開いた状態であり、第1開閉弁12は閉じた状態である。破砕部20のモータ20Gは、第1蓋60が投入口を解放した状態、分解剤が投入されていない状態、点検口30Bが蓋30Cによって閉鎖されていない状態、及び点検口40Aが蓋40Bによって閉鎖されていない状態と制御部が判別した場合、駆動しないように制御部によって制御されている。 The waste treatment device 5 first operates at least one of the first solenoid valve 14C and the second solenoid valve 14D by the control unit to remove at least one of the first predetermined amount of water and hot water from the discharge unit 14. It is supplied to the crushing unit 20. In this way, a predetermined amount of filth D and at least one of water and hot water are introduced into the crushing unit 20. At this time, the first manual on-off valve 12A is open and the first on-off valve 12 is closed. The motor 20G of the crushing unit 20 has a state in which the first lid 60 has opened the charging port, a state in which the dissolving agent has not been charged, a state in which the inspection port 30B is not closed by the lid 30C, and a state in which the inspection port 40A is closed by the lid 40B. When the control unit determines that the state is not closed, the control unit controls so as not to drive.
 第1蓋60が投入口を閉鎖した状態、分解剤が投入された状態、点検口30Bが蓋30Cによって閉鎖されている状態、及び点検口40Aが蓋40Bによって閉鎖されている状態であると制御部が判別すると、破砕部20のモータ20Gが駆動され、所定の量の汚物Dが破砕される。 Control is performed when the first lid 60 is closed, the dissolving agent is charged, the inspection port 30B is closed by the lid 30C, and the inspection port 40A is closed by the lid 40B. When the unit is determined, the motor 20G of the crushing unit 20 is driven, and a predetermined amount of the waste D is crushed.
 このとき、制御部はモータ20Gの第1負荷の大きさに基づいて投入された所定の量の汚物Dの量を推定する。具体的には、制御部によって、破砕部20に係る第1負荷(すなわち、モータ20Gの消費電力量)を検出し、第1負荷が所定値を超えたときに汚物Dを破砕しているものとし、第1負荷が所定値を超えている時間に基づいて汚物Dの量を推定する。所定の量の汚物Dは破砕部20で破砕され破砕物Cになる。制御部は、第1負荷の大きさに対応する信号に基づいて分解剤投入装置13を動作させて、所定の量の分解剤をシュート21に投入する。シュート21に投入された所定の量の分解剤はミキサ70に流入する。 At this time, the control unit estimates the amount of the predetermined amount of filth D input based on the magnitude of the first load of the motor 20G. Specifically, the control unit detects the first load (that is, the power consumption of the motor 20G) related to the crushing unit 20 and crushes the waste D when the first load exceeds a predetermined value. Then, the amount of the waste D is estimated based on the time when the first load exceeds the predetermined value. A predetermined amount of filth D is crushed in the crushing unit 20 to become crushed material C. The control unit operates the decomposing agent introducing device 13 based on the signal corresponding to the magnitude of the first load, and injects a predetermined amount of the decomposing agent into the chute 21. A predetermined amount of the decomposing agent supplied to the chute 21 flows into the mixer 70.
 次に、ミキサ70で、破砕物C、第1所定量の水及び湯の少なくともいずれか一方、及び所定の量の分解剤を攪拌して、水分を吸収保持したポリマーと分解剤とを反応させて、ポリマーが吸収保持した水分を取り出す。こうして、ミキサ70では、破砕物Cと、水及び湯の少なくともいずれか一方と、所定の量の分解剤とを攪拌して攪拌物Sにする。 Next, in the mixer 70, the crushed material C, at least one of the first predetermined amount of water and hot water, and the predetermined amount of the decomposer are stirred, and the polymer having absorbed and retained the water is reacted with the decomposer. To take out the water absorbed and retained by the polymer. In this way, in the mixer 70, the crushed material C, at least one of water and hot water, and a predetermined amount of the decomposing agent are stirred to form the stirred material S.
 このとき、制御部によって、ミキサ70のモータ70Aに係る第2負荷を検出する。具体的には、このとき検出される第2負荷の大きさは、モータ70Aの消費電流の大きさである。 At this time, the controller detects the second load related to the motor 70A of the mixer 70. Specifically, the magnitude of the second load detected at this time is the magnitude of the current consumption of the motor 70A.
 制御部はモータ70Aの第2負荷の大きさが所定の時間が経過しても所定値以下でない(すなわち、攪拌物Sのポリマーと分解剤との反応が十分進んでいない)と判別すると、分解剤を分解剤投入装置13から追加して投入するように分解剤投入装置13を制御する。このとき、モータ70Aは継続して駆動しており、ミキサ70において攪拌物Sのポリマーと分解剤との反応をさらに進めることができる。こうして、ミキサ70では、破砕物Cと、第1所定量の水及び湯の少なくともいずれか一方と、分解剤とを攪拌し、破砕物Cを攪拌物Sにし、攪拌物Sのポリマーと分解剤との反応をさらに進めることができる。 If the control unit determines that the magnitude of the second load of the motor 70A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the agitated product S and the decomposing agent has not sufficiently proceeded), the control unit decomposes. The disintegrating agent injecting device 13 is controlled so that an agent is additionally injected from the injecting agent injecting device 13. At this time, the motor 70A is continuously driven, and the mixer 70 can further promote the reaction between the polymer of the agitated substance S and the decomposing agent. Thus, in the mixer 70, the crushed material C, at least one of the first predetermined amount of water and hot water, and the decomposing agent are agitated, and the crushed material C is converted into the agitated material S. The reaction with can be further advanced.
 次に、モータ70Aの消費電流の大きさ(すなわち、第2負荷の大きさ)が所定値以下であり、第1グループG1が空の状態でなく、攪拌物Sのみが有り、第2グループG2内が空の状態であると制御部が判別すると、閉じた状態の第1開閉弁12が制御部によって開いた状態にされる。すると、排出路11を介して攪拌物Sが希釈槽30内に流入する。 Next, the magnitude of the current consumption of the motor 70A (that is, the magnitude of the second load) is equal to or less than a predetermined value, the first group G1 is not empty, only the agitated material S exists, and the second group G2 When the control unit determines that the inside is empty, the first open / close valve 12 in the closed state is opened by the control unit. Then, the agitated material S flows into the dilution tank 30 via the discharge path 11.
 このとき、制御部によって吐出部14の第1電磁弁14C及び第2電磁弁14Dを動作させて吐出部14から第2所定量の水及び湯の少なくともいずれか一方を破砕部20に供給する。第2所定量の水及び湯の少なくともいずれか一方は、攪拌物Sの量に対して所定の量である。このとき、破砕部20のモータ20G、及びミキサ70のモータ70Aは駆動している。これによって、ミキサ70内の攪拌物Sを希釈槽30内に確実に搬送しつつ破砕部20内及びミキサ70内を洗浄することができる。第1通気路17は、希釈槽30に破砕物C及び第2所定量の水及び湯の少なくともいずれか一方が流入する際、希釈槽30内が正圧になることを抑える。第2開閉弁16は、第2所定量の水及び湯の少なくともいずれか一方と攪拌物Sとが希釈槽30に流入するときから閉じた状態であり、第2手動開閉弁16Aは開いた状態である。 At this time, the first electromagnetic valve 14C and the second electromagnetic valve 14D of the discharge unit 14 are operated by the control unit to supply at least one of the second predetermined amount of water and hot water from the discharge unit 14 to the crushing unit 20. At least one of the second predetermined amount of water and hot water is a predetermined amount with respect to the amount of the stirring object S. At this time, the motor 20G of the crushing unit 20 and the motor 70A of the mixer 70 are being driven. Thus, the inside of the crushing unit 20 and the inside of the mixer 70 can be washed while the stirred material S in the mixer 70 is surely conveyed into the dilution tank 30. The first ventilation path 17 suppresses the inside of the dilution tank 30 from becoming a positive pressure when at least one of the crushed material C and the second predetermined amount of water and hot water flows into the dilution tank 30. The second on-off valve 16 is in a closed state when at least one of the second predetermined amount of water and hot water and the agitated material S flow into the dilution tank 30, and the second manual on-off valve 16A is in an open state. It is.
 第1グループG1ではおよそ90秒間で所定の量の汚物Dを攪拌物Sにし、攪拌物Sと第2所定量の水及び湯の少なくともいずれか一方が第2グループG2に流入する。制御部は、第1グループG1内が空でない状態から空の状態に変化したことを検知すると、開いた状態の第1開閉弁12が閉じた状態にする。こうして、第1グループG1は再び所定の量の汚物Dを攪拌物Sにすることができる状態になる。つまり、汚物処理装置5は、第1グループG1と第2グループG2とで並行して汚物Dや攪拌物S等の汚物の分離処理を行うことができる。これによって、汚物処理装置5は全体としての汚物Dの処理量を増やすことができる。 で は In the first group G1, a predetermined amount of the filth D is made into the stirrer S in about 90 seconds, and the stirrer S and at least one of the second predetermined amount of water and hot water flow into the second group G2. When the control unit detects that the inside of the first group G1 has changed from a non-empty state to an empty state, the control unit sets the open first on-off valve 12 to a closed state. Thus, the first group G1 is again in a state in which a predetermined amount of the waste D can be made into the agitated material S. That is, the waste disposal apparatus 5 can perform the separation processing of the waste such as the waste D and the stirrer S in parallel in the first group G1 and the second group G2. Thereby, the waste disposal apparatus 5 can increase the throughput of the waste D as a whole.
 次に、第2所定量の水及び湯の少なくともいずれか一方と攪拌物Sとを希釈槽30で希釈して攪拌物Sを希釈物Tにする。このとき、第2手動開閉弁16Aは開いた状態であり、第2開閉弁16は閉じた状態である。先ず、制御部によって希釈槽30のモータ30Aの駆動が開始される。これによって、希釈槽30のプロペラ(図示せず)が回転し、第2所定量の水及び湯の少なくともいずれか一方と攪拌物Sとが攪拌され、攪拌物Sが希釈されて希釈物Tになる。これによって、攪拌物Sに含まれる分解剤のCa(カルシウム)やCl(塩素)の攪拌物Sにおける濃度を希釈物Tにすることによって小さくすることができ、下水管にCaの成分が付着して固まったり、Clによって下水管が腐食したりすることを抑えることができる。 Next, at least one of the second predetermined amount of water and hot water and the stirred material S are diluted in the dilution tank 30 to make the stirred material S a diluted material T. At this time, the second manual on-off valve 16A is open and the second on-off valve 16 is closed. First, the drive of the motor 30A of the dilution tank 30 is started by the control unit. As a result, the propeller (not shown) of the dilution tank 30 rotates, and the second predetermined amount of at least one of water and hot water and the agitated material S are agitated. Become. Accordingly, the concentration of Ca (calcium) or Cl (chlorine) of the decomposing agent contained in the agitated material S in the agitated material S can be reduced by using the diluent T, and the Ca component adheres to the sewer pipe. It is possible to suppress that the sewer pipe is corroded due to hardening or Cl.
 このとき、制御部によって、希釈槽30のモータ30Aに係る第3負荷を監視する。具体的には、このとき検出される第3負荷の大きさは、希釈槽30のモータ30Aの消費電流の大きさである。 、 At this time, the third load on the motor 30A of the dilution tank 30 is monitored by the control unit. Specifically, the magnitude of the third load detected at this time is the magnitude of the current consumption of the motor 30A of the dilution tank 30.
 制御部は、所定の時間が経過してもモータ30Aの第3負荷の大きさが所定値以下でない(すなわち、希釈物Tのポリマーと分解剤との反応が十分進んでいない)と判別すると、分解剤を分解剤投入装置13から追加して投入するように分解剤投入装置13を制御する。このとき、希釈槽30のモータ30Aも継続して駆動しており、希釈槽30において希釈物Tのポリマーと分解剤との反応をさらに進めることができる。こうして、希釈槽30では、攪拌物Sと第2所定量の水及び湯の少なくともいずれか一方とが攪拌され、攪拌物Sが希釈されてポリマーと分解剤との反応が進んだ希釈物Tになる。希釈槽30に分解剤投入口を形成し、この分解剤投入口にも分解剤投入装置13から分解剤を投入することができる構成としてもよい。これによって、分解剤を追加して投入する際に、希釈槽30に分解剤を直接投入することができる。 If the control unit determines that the magnitude of the third load of the motor 30A is not less than or equal to the predetermined value even after the predetermined time has elapsed (that is, the reaction between the polymer of the diluent T and the decomposer has not sufficiently proceeded), The decomposing agent input device 13 is controlled so that the decomposing agent is additionally input from the decomposing agent input device 13. At this time, the motor 30A of the dilution tank 30 is also continuously driven, and the reaction between the polymer of the diluent T and the decomposing agent can be further advanced in the dilution tank 30. Thus, in the dilution tank 30, the agitated material S and at least one of the second predetermined amount of water and hot water are agitated, and the agitated material S is diluted to the diluted material T in which the reaction between the polymer and the decomposing agent has progressed. Become. A configuration may be adopted in which a decomposing agent inlet is formed in the dilution tank 30 and a decomposing agent can be supplied from the decomposing agent input device 13 also to this decomposing agent inlet. Thus, when the additional decomposing agent is added, the decomposing agent can be directly injected into the dilution tank 30.
 次に、希釈物Tから固形分を分離する。先ず、制御部によって、モータ30Aの消費電流の大きさ(すなわち、第3負荷の大きさ)が所定値以下であり、第2グループG2内が空の状態でなく、第3グループG3内が空の状態であると制御部が判別すると、閉じた状態の第2開閉弁16が制御部によって開いた状態にされる。すると、希釈物Tが希釈槽30から分離部40に向けて流れる。 Next, the solid content is separated from the diluent T. First, the control unit determines that the magnitude of the current consumption of the motor 30A (that is, the magnitude of the third load) is equal to or smaller than a predetermined value, and that the second group G2 is not empty and the third group G3 is empty. When the control unit determines that the second open / close valve 16 is in the closed state, the second open / close valve 16 in the closed state is opened by the control unit. Then, the diluent T flows from the dilution tank 30 toward the separation unit 40.
 第2グループG2ではおよそ85秒間で攪拌物Sを希釈物Tにし、希釈物Tが第3グループG3に流入する。制御部は、第2グループG2内が空でない状態から空の状態に変化したことを検知すると、開いた状態の第2開閉弁16を閉じた状態にする。こうして、第2グループG2は再び攪拌物Sを希釈物Tにすることができる状態になる。つまり、汚物処理装置5は、第1グループG1、第2グループG2、及び第3グループG3で並行して汚物D、攪拌物S、及び希釈物T等の汚物の分離処理を行うことができる。これによって、汚物処理装置5は全体としての汚物Dの処理量を増やすことができる。 {Circle around (2)} In the second group G2, the mixture S is turned into the diluent T in about 85 seconds, and the diluent T flows into the third group G3. Upon detecting that the inside of the second group G2 has changed from a non-empty state to an empty state, the control unit closes the open second on-off valve 16. In this way, the second group G2 is in a state where the stirred substance S can be turned into the diluted substance T again. In other words, the waste disposal apparatus 5 can perform the separation processing of the waste such as the waste D, the agitated material S, and the diluent T in parallel in the first group G1, the second group G2, and the third group G3. Thereby, the waste disposal apparatus 5 can increase the throughput of the waste D as a whole.
 汚物処理装置5は第1蓋60で投入口が閉鎖されている。このため、第1通気路17の負圧解消部17Aから第1通気路17内に空気を取り込むことによって希釈槽30内が負圧になることを抑え、これによって、希釈物Tを希釈槽30から分離部40に向けて良好に流すことができる。制御部によって分離部40のモータ40Cの駆動が開始される。このとき、制御部によって吸気部19Aの動作も開始される。 投入 The input port of the waste disposal apparatus 5 is closed by the first lid 60. For this reason, by taking in air from the negative pressure eliminating portion 17A of the first ventilation path 17 into the first ventilation path 17, it is possible to prevent the inside of the dilution tank 30 from becoming a negative pressure. , And can be satisfactorily flowed toward the separation section 40. The drive of the motor 40C of the separation unit 40 is started by the control unit. At this time, the operation of the suction unit 19A is also started by the control unit.
 排水路15に流入した希釈物Tは、分離部40に流入し、モータ40Cが駆動することによって、希釈物Tの固形分が固形分排出部40Dから排出される。固形分排出部40Dから排出された希釈物Tの固形分は、固形分排出部40Dの先端部に取り付けられた回収袋40Eに取り込まれる。このとき、第3通気路19及び吸気部19Aによって、固形分排出部40Dで生じる臭気が投入部10に導かれる。希釈物Tの水分はトラップ15Aを通過して下水管(図示せず)に流れる。 The diluent T that has flowed into the drainage channel 15 flows into the separation unit 40, and the solid content of the diluent T is discharged from the solid discharge unit 40D by driving the motor 40C. The solids of the diluent T discharged from the solids discharge unit 40D are taken into the collection bag 40E attached to the tip of the solids discharge unit 40D. At this time, the odor generated in the solids discharge section 40D is guided to the input section 10 by the third ventilation path 19 and the suction section 19A. The water of the diluent T flows through the trap 15A to a drain (not shown).
 分離部40は第2通気路18を介して第1通気路17に連通している。これによって、分離部40内が負圧になることが抑えられ、希釈物Tの水分を分離部40から下水管に向けて良好に流すことができる。トラップ15A内に残留する希釈物Tの水分は、トラップ15Aに接続されたゼット排水部(図示せず)からトラップ15Aに向けて水を勢いよく供給することによって下水管に確実に搬送される。第3グループG3ではおよそ80秒間で希釈物Tから固形分を分離して、希釈物Tの水分を下水管に流すことができる。第3グループG3内が空の状態でない状態から空の状態に変化すると、第3グループG3は希釈物Tからの固形分の分離を再び行うことができる状態になる。 The separating section 40 is in communication with the first ventilation path 17 via the second ventilation path 18. Thereby, the inside of the separation unit 40 is suppressed from being negative pressure, and the water of the diluent T can be satisfactorily flowed from the separation unit 40 toward the sewer pipe. The water of the diluent T remaining in the trap 15A is surely conveyed to the sewer pipe by vigorously supplying water to the trap 15A from a jet drain (not shown) connected to the trap 15A. In the third group G3, the solids can be separated from the diluent T in about 80 seconds, and the water of the diluent T can be flown to the sewer. When the inside of the third group G3 changes from a state that is not empty to an empty state, the third group G3 is in a state where the solids can be separated from the diluent T again.
 第3グループG3の処理時間は第1グループG1及び第2グループG2の処理時間よりも短く、第2グループG2の処理時間は第1グループG1の処理時間よりも短い。このため、各グループで並行して汚物D、攪拌物S、及び希釈物T等の汚物の分離処理を行う場合、上流側のグループよりも下流側のグループの処理が早く終わるため、上流側のグループにおいて処理が終了した後、直ちに下流側のグループに攪拌物S、及び希釈物Tを流入させることができる。 処理 The processing time of the third group G3 is shorter than the processing time of the first group G1 and the second group G2, and the processing time of the second group G2 is shorter than the processing time of the first group G1. For this reason, when the wastes such as the wastes D, the agitated materials S, and the diluents T are separated in parallel in each group, the processing in the downstream group ends earlier than the processing in the upstream group. Immediately after the processing is completed in the group, the stirred substance S and the diluted substance T can flow into the downstream group.
 希釈物Tからの固形分の分離が終了した後、操作部(図示せず)を操作することによって、破砕部20、ミキサ70、希釈槽30、及び分離部40の各モータ20G,70A,30A,40Cの駆動が停止される。各モータ20G,70A,30A,40Cの駆動が停止した後、所定の時間が経過したとき、制御部は吐出部14の第2吐出部14Bから湯が供給されるように制御する。このとき、制御部によって、破砕部20、ミキサ70、希釈槽30、及び分離部40の各モータ20G,70A,30A,40Cを駆動させ、第1開閉弁12、及び第2開閉弁16開いた状態にする。これによって、汚物処理装置5は、汚物処理装置5内に汚物D、破砕物C、攪拌物S、及び希釈物T等が残らないように洗浄して、汚物処理装置5内にCaの成分が付着して固まったり、Clによって汚物処理装置5内が腐食したりすることを抑えることができる。 After the separation of the solid content from the diluent T is completed, by operating an operation unit (not shown), the motors 20G, 70A, 30A of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are operated. , 40C are stopped. When a predetermined time elapses after the driving of each of the motors 20G, 70A, 30A, and 40C is stopped, the control unit controls so that hot water is supplied from the second discharge unit 14B of the discharge unit 14. At this time, the motors 20G, 70A, 30A, and 40C of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are driven by the control unit, and the first on-off valve 12 and the second on-off valve 16 are opened. State. Thereby, the waste disposal apparatus 5 is cleaned so that the waste D, the crushed substance C, the agitated substance S, the diluent T, and the like do not remain in the waste disposal apparatus 5, and the Ca component is contained in the waste disposal apparatus 5. It is possible to suppress adhesion and solidification, and corrosion of the inside of the waste disposal apparatus 5 by Cl.
 次に、各グループ(第1グループG1、第2グループG2、第3グループG3)のいずれか1つを交換する場合について説明する。第1グループG1を取り外す場合、先ず、第1手動開閉弁12A、第1開閉弁12を閉じた状態にする。そして、第1接続部11Aにおいて排出路11を第1手動開閉弁12A側と第1開閉弁12側とに切り離す。次に、投入部10から第1通気路17の一端、及び第3通気路19の一端を取り外す。破砕部20はモータ20Gが汚物処理装置5内に置き残された状態で取り外される。ミキサ70はモータ70Aが汚物処理装置5内に置き残された状態で取り外される。 Next, a case where one of the groups (the first group G1, the second group G2, and the third group G3) is exchanged will be described. When removing the first group G1, first, the first manual on-off valve 12A and the first on-off valve 12 are closed. Then, the discharge path 11 is separated into the first manual opening / closing valve 12A side and the first opening / closing valve 12 side at the first connection portion 11A. Next, one end of the first ventilation path 17 and one end of the third ventilation path 19 are removed from the charging section 10. The crushing unit 20 is removed with the motor 20G left in the waste disposal apparatus 5. The mixer 70 is removed with the motor 70A left in the waste disposal apparatus 5.
 第2グループG2を取り外す場合、先ず、第1手動開閉弁12A、第1開閉弁12、第2手動開閉弁16A、及び第2開閉弁16を閉じた状態にする。次に、第1接続部11Aにおいて排出路11を第1手動開閉弁12A側と第1開閉弁12側とに切り離し、第2接続部15Bにおいて、排水路15を第2手動開閉弁16A側と第2開閉弁16側とに切り離す。次に、希釈槽30から第1通気路17の他端を取り外す。希釈槽30は、モータ30Aが汚物処理装置5内に置き残された状態で取り外される。 When removing the second group G2, first, the first manual on-off valve 12A, the first on-off valve 12, the second manual on-off valve 16A, and the second on-off valve 16 are closed. Next, at the first connection portion 11A, the discharge passage 11 is separated into the first manual opening / closing valve 12A side and the first opening / closing valve 12 side. At the second connection portion 15B, the drain passage 15 is connected to the second manual opening / closing valve 16A side. Disconnect from the second on-off valve 16 side. Next, the other end of the first ventilation path 17 is removed from the dilution tank 30. The dilution tank 30 is removed in a state where the motor 30A is left in the waste disposal apparatus 5.
 第3グループG3を取り外す場合、先ず、第2手動開閉弁16A、及び第2開閉弁16を閉じた状態にする。次に、第2接続部15Bにおいて、排水路15を第2手動開閉弁16A側と第2開閉弁16側とに切り離す。次に、分離部40から第2通気路18の他端を取り外し、固形分排出部40Dから第3通気路19の他端を取り外す。分離部40は、モータ40Cが汚物処理装置5内に置き残された状態で取り外される。第1通気路17、第2通気路18、及び第3通気路19は各グループのいずれを交換する場合でも、汚物処理装置5内に置き残される。こうして、汚物処理装置5は、第1グループG1、第2グループG2、及び第3グループG3において、汚物D、破砕物C、攪拌物S、及び希釈物T等の汚物に直接触れる部分のみを取り外すことができる。汚物処理装置5は、第1グループG1、第2グループG2、及び第3グループG3のグループ毎に着脱自在である。 When removing the third group G3, first, the second manual on-off valve 16A and the second on-off valve 16 are closed. Next, at the second connection portion 15B, the drainage channel 15 is separated into the second manual on-off valve 16A side and the second on-off valve 16 side. Next, the other end of the second ventilation path 18 is removed from the separation section 40, and the other end of the third ventilation path 19 is removed from the solid content discharge section 40D. The separation unit 40 is removed with the motor 40C left in the waste disposal apparatus 5. The first ventilation path 17, the second ventilation path 18, and the third ventilation path 19 are left in the waste disposal apparatus 5 when any of the groups is replaced. In this way, the waste disposal apparatus 5 removes only the portion of the first group G1, the second group G2, and the third group G3 that directly touches the waste such as the waste D, the crushed material C, the agitated material S, and the diluent T. be able to. The waste disposal apparatus 5 is detachable for each of a first group G1, a second group G2, and a third group G3.
 このように、第3の汚物処理装置5は、下流側の処理部の一回の処理で処理できる処理量が上流側の処理部が一回の処理で処理できる処理量以上であるため、上流側の処理部によって処理された汚物D、破砕物C、攪拌物S、及び希釈物T等の汚物が下流側の処理部に直ちに流入することができる。このため、汚物処理装置5は、各処理部の間に中間槽等を設けずに済む。 As described above, the third waste disposal apparatus 5 is configured such that the processing amount that can be processed by one processing of the downstream processing unit is equal to or larger than the processing amount that can be processed by the upstream processing unit by one processing. The filth, such as the filth D, the crushed material C, the agitated material S, and the diluent T, which have been processed by the processing unit on the side, can immediately flow into the processing unit on the downstream side. For this reason, the waste disposal apparatus 5 does not need to provide an intermediate tank or the like between the processing units.
 したがって、第3の汚物処理装置5はより小型化することができる。 Thus, the third waste disposal apparatus 5 can be downsized.
 第3の汚物処理装置5は、1つ及び複数の少なくともいずれか一方の処理部で構成される第1グループG1、第2グループG2、及び第3グループG3を構成し、第1グループG1、第2グループG2、及び第3グループG3の処理時間は上流側のグループよりも下流側のグループが短い。このため、汚物処理装置5は、第1グループG1、第2グループG2、及び第3グループG3を並列に動作させることができ、これによって、汚物処理装置5は全体としての汚物Dの処理量を増やすことができる。 The third sewage treatment apparatus 5 forms a first group G1, a second group G2, and a third group G3, each of which includes one and a plurality of at least one processing unit. The processing times of the second group G2 and the third group G3 are shorter in the downstream group than in the upstream group. For this reason, the waste disposal apparatus 5 can operate the first group G1, the second group G2, and the third group G3 in parallel, whereby the waste disposal apparatus 5 can reduce the amount of waste D processed as a whole. Can be increased.
 第3の汚物処理装置5は、第1グループG1、第2グループG2、及び第3グループG3同士を接続する第1接続部11Aに第1開閉弁12が設けられ、第2接続部15Bに第2開閉弁16が設けられている。このため、汚物処理装置5は、第1開閉弁12、及び第2開閉弁16によって第1グループG1、第2グループG2、及び第3グループG3において汚物D、攪拌物S、及び希釈物T等の汚物の処理を分けて、且つ同時に行うことができる。 In the third waste disposal apparatus 5, the first connection portion 11A connecting the first group G1, the second group G2, and the third group G3 is provided with the first on-off valve 12, and the second connection portion 15B is provided with the first on-off valve 12. Two on-off valves 16 are provided. For this reason, the waste disposal apparatus 5 uses the first opening / closing valve 12 and the second opening / closing valve 16 to control the waste D, the agitated material S, and the diluent T in the first group G1, the second group G2, and the third group G3. Can be performed separately and simultaneously.
 第3の汚物処理装置5は、第1グループG1、第2グループG2、及び第3グループG3毎に着脱自在である。このため、汚物処理装置5は、部品の取り換え等のメンテナンスを容易に行うことができる。 The third waste disposal apparatus 5 is detachable for each of the first group G1, the second group G2, and the third group G3. For this reason, the waste disposal apparatus 5 can easily perform maintenance such as replacement of parts.
<実施形態6>
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6は、被処理物としての使用済の紙おむつDdを処理する装置である。紙おむつは、パルプ、プラスティック、高吸水性ポリマー(SAP,super absorbent polymer、以下単にポリマーと表記する)等で形成されている。使用済みの紙おむつはパルプやポリマーにし尿等の汚物の水分が吸収される。水分を吸収したポリマーは処理剤を用いて処理を行うことによって吸水性能が抑制される。具体的には、処理剤は、塩化カルシウム(CaCl2)や酢酸カルシウム(Ca(CH3COO)2)等の2価の金属イオンを含んだ薬剤であり、これらとポリマーとを反応させることによって、水分を吸収したポリマーから水分が分離されるとともに、水分を分離されたポリマーは再び水分を吸収不能な不可逆状態にされる。使用済みの紙おむつDdに水分を吸収していないポリマーが含まれている場合であっても、処理剤を用いて処理を行うことによって、水分を吸収不能な状態にされる。
<Embodiment 6>
The waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus is an apparatus for processing a used paper diaper Dd as an object to be treated. The disposable diaper is made of pulp, plastic, superabsorbent polymer (SAP, superabsorbent polymer, hereinafter simply referred to as polymer), or the like. Used disposable diapers are converted into pulp or polymer, and the moisture of dirt such as urine is absorbed. The water-absorbing performance of the polymer that has absorbed water is suppressed by performing the treatment using the treating agent. Specifically, the treating agent is a chemical containing divalent metal ions such as calcium chloride (CaCl 2 ) and calcium acetate (Ca (CH 3 COO) 2 ), and by reacting these with a polymer. Water is separated from the polymer that has absorbed the water, and the polymer from which the water has been separated is again brought into an irreversible state in which the water cannot be absorbed. Even in the case where the used disposable diaper Dd contains a polymer that does not absorb moisture, the treatment with the treatment agent renders it impossible to absorb moisture.
 第4及び第5の汚物処理装置6は、図6に示すように、投入部10、処理部90、及び制御部50を備えている。投入部10は吸水性のポリマーを有した被処理物としての紙おむつDdが投入される。処理部90は処理剤を用いて紙おむつDdの処理を行う。本実施形態において、処理部90は破砕部20、ミキサ70、希釈槽30、及び分離部40を有して構成されている。これら破砕部20、ミキサ70、希釈槽30、及び分離部40は駆動部としてのモータ20G,70A,30A,40Cによってそれぞれ駆動される。制御部50は投入部10から投入された紙おむつDdの状態を判定する判定部51を有するとともに、判定部51が判定した紙おむつDdの状態に基づいて処理剤の投入量を決定する。 The fourth and fifth filth disposal apparatuses 6 include an input unit 10, a processing unit 90, and a control unit 50, as shown in FIG. The dispensing section 10 is charged with a disposable diaper Dd as a processing object having a water-absorbing polymer. The processing unit 90 performs the processing of the paper diaper Dd using the processing agent. In the present embodiment, the processing section 90 includes the crushing section 20, the mixer 70, the dilution tank 30, and the separation section 40. The crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 are driven by motors 20G, 70A, 30A, and 40C as driving units, respectively. The control unit 50 includes a determination unit 51 that determines the state of the paper diaper Dd input from the input unit 10, and determines the amount of the processing agent to be input based on the state of the paper diaper Dd determined by the determination unit 51.
 本実施形態において、汚物処理装置6は、図6及び図7に示すように、処理剤投入部23、計測部52、報知部53、記憶部54、及び送信部55を備えている。処理剤投入部23は処理剤を処理部90に投入する。計測部52は投入部10から投入された紙おむつDdの個数を計測する。報知部53は汚物処理装置6の稼働状況に関する情報を報知する。記憶部54は汚物処理装置6の稼働状況に関する情報を記憶する。送信部55は汚物処理装置6の稼働状況に関する情報を外部に送信する。 に お い て In the present embodiment, the waste disposal apparatus 6 includes a treatment agent introduction unit 23, a measurement unit 52, a notification unit 53, a storage unit 54, and a transmission unit 55, as shown in FIGS. The processing agent input section 23 inputs the processing agent into the processing section 90. The measuring unit 52 measures the number of the disposable diapers Dd input from the input unit 10. The notification unit 53 reports information on the operation status of the waste disposal apparatus 6. The storage unit 54 stores information on the operation status of the waste disposal apparatus 6. The transmitting unit 55 transmits information on the operation status of the waste disposal apparatus 6 to the outside.
 投入部10は、図6に示すように、上下方向に延びる筒状をなしている。投入部10の上端は使用済みの紙おむつDdが投入される投入口とされている。投入部10の上端には投入口を開閉する第1蓋60が設けられている。投入部10には図示しない脱臭装置が設けられている。 (6) The loading section 10 has a tubular shape extending in the vertical direction as shown in FIG. The upper end of the input unit 10 is an input port into which a used paper diaper Dd is input. At the upper end of the charging section 10, a first lid 60 for opening and closing the charging port is provided. The charging unit 10 is provided with a deodorizing device (not shown).
 図6に示すように、投入部10には吐出部14が設けられている。吐出部14は、汚物処理装置6による各処理や洗浄に使用する水を供給する。吐出部14には電磁弁14Eが設けられている。電磁弁14Eは制御部50によって開閉動作が制御される。本実施形態において、吐出部14は水のみならず、40℃から90℃程度の湯を供給することも可能である。例えば、一般的な紙おむつには粘着剤が使用されている。湯を使用して各処理を行うことで、紙おむつの粘着剤をより軟化させ、装置への付着を抑制することができる。湯を使用した装置の洗浄を定期的に行うことで、装置内に付着した紙おむつの固形分を洗浄して除去することができる。湯を使用した洗浄によって装置内の殺菌を行うこともできる。本実施形態の汚物処理装置6では、制御部50の制御によって、水及び湯の少なくともいずれか一方を吐出部14から都度選択的に供給することができる。但し、以下の説明では、吐出部14から供給される水及び湯の少なくともいずれか一方については単に「水」として説明する。 吐出 As shown in FIG. 6, the charging section 10 is provided with a discharge section 14. The discharge unit 14 supplies water used for each processing and cleaning by the waste disposal apparatus 6. The discharge unit 14 is provided with a solenoid valve 14E. The opening and closing operation of the solenoid valve 14E is controlled by the control unit 50. In the present embodiment, the discharge section 14 can supply not only water but also hot water of about 40 ° C. to 90 ° C. For example, an adhesive is used for a general disposable diaper. By performing each treatment using hot water, the pressure-sensitive adhesive of the disposable diaper can be softened more and the adhesion to the device can be suppressed. By periodically cleaning the device using hot water, the solid content of the disposable diaper attached to the device can be removed by cleaning. It is also possible to sterilize the inside of the apparatus by washing with hot water. In the waste disposal apparatus 6 of the present embodiment, under the control of the control unit 50, at least one of water and hot water can be selectively supplied from the discharge unit 14 each time. However, in the following description, at least one of water and hot water supplied from the discharge unit 14 will be described simply as “water”.
 処理剤投入部23は処理部90に処理剤を投入する。処理剤投入部23は、後述する処理部90のシュート21に設けられており、このシュート21内に処理剤を投入する。処理剤投入部23は、例えば、公知の定量フィーダー等が用いられる。本実施形態の場合、処理剤投入部23は、制御部50によって制御され、制御部50が決定した投入量で処理剤を投入する。処理剤投入部23は、紙おむつDdの状態に基づいて決定された量の固体の処理剤を投入するように、制御部50によって制御される。 The processing agent input section 23 inputs the processing agent into the processing section 90. The processing agent charging section 23 is provided on a chute 21 of a processing section 90 described later, and charges the processing agent into the chute 21. For the treatment agent input section 23, for example, a known quantitative feeder or the like is used. In the case of the present embodiment, the processing agent input unit 23 is controlled by the control unit 50, and inputs the processing agent at the input amount determined by the control unit 50. The processing agent input unit 23 is controlled by the control unit 50 so as to input an amount of the solid processing agent determined based on the state of the paper diaper Dd.
 本実施形態の処理剤投入部23は、第1処理剤投入部23A及び第2処理剤投入部23Bを有している。第1処理剤投入部23Aは酢酸カルシウムを含む処理剤を投入する。第2処理剤投入部23Bは塩化カルシウムを含む処理剤を投入する。処理剤投入部23は、制御部50の制御によってこれら2つの処理剤投入部23A,23Bから、酢酸カルシウムを含む処理剤と、塩化カルシウムを含む処理剤とを所望の比率で投入し得るように構成されている。具体的には、汚物処理装置6の通常の運転では、制御部50は、酢酸カルシウムが所定の比率となる形態で、酢酸カルシウムを含む処理剤と塩化カルシウムを含む処理剤との両方の処理剤を第1処理剤投入部23A及び第2処理剤投入部23Bのそれぞれから投入する制御を実行する。一方、後述する処理部90のミキサ70、希釈槽30、及び分離部40の各洗浄モードにおいて処理剤を投入する場合には、制御部50は、第1処理剤投入部23Aからの酢酸カルシウムを含む処理剤のみを投入する制御を実行する。 処理 The processing agent input section 23 of the present embodiment has a first processing agent input section 23A and a second processing agent input section 23B. The first processing agent input section 23A inputs a processing agent containing calcium acetate. The second processing agent input section 23B inputs the processing agent containing calcium chloride. Under the control of the control unit 50, the processing agent input unit 23 can input the processing agent including calcium acetate and the processing agent including calcium chloride at a desired ratio from the two processing agent input units 23A and 23B. It is configured. Specifically, in the normal operation of the waste disposal apparatus 6, the control unit 50 controls both the treatment agent containing calcium acetate and the treatment agent containing calcium chloride in a form in which calcium acetate has a predetermined ratio. Is supplied from each of the first processing agent charging section 23A and the second processing agent charging section 23B. On the other hand, when the processing agent is supplied in each of the cleaning modes of the mixer 70, the dilution tank 30, and the separation unit 40 of the processing unit 90 described below, the control unit 50 removes the calcium acetate from the first processing agent input unit 23A. The control for inputting only the processing agent including the control agent is executed.
 図6に示すように、処理部90は、処理の上流側から、破砕部20、ミキサ70、希釈槽30、及び分離部40の順に配置されている。最も上流側に配置されている破砕部20は、投入部10の下端に連結されており、投入部10から投入された紙おむつDdが導入される。 As shown in FIG. 6, the processing unit 90 is arranged in the order of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 from the upstream side of the processing. The crushing unit 20 arranged at the most upstream side is connected to the lower end of the input unit 10, and the paper diaper Dd input from the input unit 10 is introduced.
 破砕部20は、上下に貫通して形成されており、内部に破砕用回転刃(図示せず)を回転自在に配置している。本実施形態の破砕部20は、モータ20Gによって回転刃(図示せず)を内部で回転させ、被処理物としての紙おむつDdを構成するパルプ、プラスティック、ポリマー等を破砕物Cに破砕する処理を行う。破砕部20としては、例えば、公知のディスポーザーやシュレッダー等を用いてもよい。破砕部20は、回転刃を有するものに限らず、往復動する刃を有するものや回転刃と往復動刃等の異なる方式の刃を有するものであってもよい。 The crushing part 20 is formed so as to penetrate up and down, and a crushing rotary blade (not shown) is rotatably arranged inside. The crushing unit 20 according to the present embodiment performs a process in which a rotary blade (not shown) is internally rotated by a motor 20G to crush pulp, plastic, polymer, and the like, which constitute a disposable diaper Dd, as crushed materials C. Do. As the crushing unit 20, for example, a known disposer or shredder may be used. The crushing unit 20 is not limited to the one having the rotary blade, but may be one having a reciprocating blade or one having a different type of blade such as a rotary blade and a reciprocating blade.
 破砕部20のモータ20Gの駆動は制御部50によって制御される。破砕部20には、回転刃を回転させるモータ20Gの消費電流の大きさを測定する第1測定部20Hが設けられている。この第1測定部20Hが測定した消費電流の大きさに基づいて、破砕部20における処理の状況が判定部51によって判定される。この場合、第1測定部20Hは、モータ20Gの消費電力の大きさを破砕部20の運転状態に関する情報として取得する情報取得部として機能する。具体的には、第1測定部20Hが測定した消費電流の大きさを所定値と比較して、破砕部20が紙おむつDdを処理中であるか否かが判定される。詳細は後述の動作説明にて説明する。破砕部20の下端には、生成した破砕物Cをミキサ70に導くシュート21が連結されている。シュート21には、上述のように、処理剤投入部23が設けられている。 駆 動 The drive of the motor 20G of the crushing unit 20 is controlled by the control unit 50. The crushing unit 20 is provided with a first measuring unit 20H that measures the amount of current consumed by a motor 20G that rotates the rotary blade. Based on the magnitude of the current consumption measured by the first measuring unit 20H, the state of the processing in the crushing unit 20 is determined by the determining unit 51. In this case, the first measurement unit 20H functions as an information acquisition unit that acquires the amount of power consumption of the motor 20G as information on the operation state of the crushing unit 20. Specifically, the magnitude of the current consumption measured by the first measuring unit 20H is compared with a predetermined value to determine whether or not the crushing unit 20 is processing the paper diaper Dd. The details will be described later in the operation description. A chute 21 for guiding the generated crushed material C to the mixer 70 is connected to a lower end of the crushing unit 20. As described above, the chute 21 is provided with the treatment agent charging section 23.
 ミキサ70は、上部が開口して形成されており、内部に混合用回転刃(図示せず)を回転自在に配置している。ミキサ70は、上端をシュート21の下端に連結している。ミキサ70は、シュート21を経て破砕部20から導入される破砕物Cと、シュート21に設けられた処理剤投入部23から投入される処理剤とを混合して混合物Mを生成する処理を行う。本実施形態のミキサ70は、回転刃をモータ70Aによって内部(筒内)で回転することによって破砕物Cと処理剤とを混合する。ミキサ70は、回転刃を有するものに限らず、往復動する刃を有するものや回転刃と往復動刃等の異なる方式の刃を有するものであってもよい。 The mixer 70 is formed with an open top, and has a mixing rotary blade (not shown) rotatably disposed therein. The mixer 70 has an upper end connected to the lower end of the chute 21. The mixer 70 performs a process of mixing the crushed material C introduced from the crushing unit 20 via the chute 21 and the processing agent supplied from the processing agent input unit 23 provided in the chute 21 to generate a mixture M. . The mixer 70 of the present embodiment mixes the crushed material C and the processing agent by rotating the rotary blade inside (in the cylinder) by the motor 70A. The mixer 70 is not limited to the one having the rotary blade, but may be one having a reciprocating blade or one having a different type of blade such as a rotary blade and a reciprocating blade.
 ミキサ70のモータ70Aの駆動は制御部50によって制御される。ミキサ70には、回転刃を回転させるモータ70Aの消費電流の大きさを測定する第2測定部70Bが設けられている。この第2測定部70Bが測定した消費電流の大きさに基づいて、ミキサ70における処理の状況が判定部51によって判定される。この場合、第2測定部70Bはモータ70Aの消費電力の大きさをミキサ70の運転状態に関する情報として取得する情報取得部として機能する。具体的には、第2測定部70Bが測定した消費電流の大きさを2つの所定値と比較して、ミキサ70が破砕物Cを処理中であるか否かが判定される。詳細は後述の動作説明にて説明する。ミキサ70の下部側面には生成した混合物Mを希釈槽30に排出する排出路11の一端が接続されている。排出路11には排出路11を開閉する第1開閉弁12が設けられている。第1開閉弁12は制御部50によって開閉動作が制御される。第1開閉弁12は、例えば、公知の電動ボールバルブ等を有して構成される。第1開閉弁12は排出路11のミキサ70寄りの一端部側に設けられている。 The driving of the motor 70A of the mixer 70 is controlled by the control unit 50. The mixer 70 is provided with a second measuring unit 70B that measures the amount of current consumed by the motor 70A that rotates the rotary blade. Based on the magnitude of the current consumption measured by the second measuring unit 70B, the state of the processing in the mixer 70 is determined by the determining unit 51. In this case, the second measurement unit 70B functions as an information acquisition unit that acquires the amount of power consumption of the motor 70A as information on the operation state of the mixer 70. Specifically, the magnitude of the current consumption measured by the second measuring unit 70B is compared with two predetermined values to determine whether or not the mixer 70 is processing the crushed material C. The details will be described later in the operation description. One end of a discharge path 11 for discharging the generated mixture M to the dilution tank 30 is connected to a lower side surface of the mixer 70. The discharge path 11 is provided with a first on-off valve 12 for opening and closing the discharge path 11. The opening / closing operation of the first opening / closing valve 12 is controlled by the control unit 50. The first on-off valve 12 includes, for example, a known electric ball valve and the like. The first on-off valve 12 is provided at one end of the discharge path 11 near the mixer 70.
 希釈槽30は、内部の空間にプロペラ(図示せず)を回転自在に配置して形成されている。希釈槽30は、排出路11の他端が連結されている。希釈槽30は、排出路11を経てミキサ70から排出される混合物Mを水で希釈して希釈物Tを生成する。希釈槽30は、モータ30Aによって槽内のプロペラ(図示せず)を回転させつつ、混合物Mを希釈する。モータ30Aの駆動は制御部50によって制御される。希釈槽30には、プロペラを回転させるモータ30Aの消費電流の大きさを測定する第3測定部30Dが設けられている。この第3測定部30Dが測定した消費電流の大きさに基づいて、希釈槽30における処理の状況が判定部51によって判定される。この場合、第3測定部30Dは、モータ30Aの消費電力の大きさを希釈槽30の運転状態に関する情報として取得する情報取得部として機能する。具体的には、第3測定部30Dが測定した消費電流の大きさを2つの所定値と比較して、希釈槽30が混合物Mを処理中であるか否かが判定される。詳細は後述の動作説明にて説明する。希釈槽30には、生成した希釈物Tを分離部40に排出する排水路15の一端が接続されている。排水路15には、排水路15を開閉する第2開閉弁16が設けられている。第2開閉弁16は制御部50によって開閉動作が制御される。第2開閉弁16は、例えば、第1開閉弁12と同様に、公知の電動ボールバルブ等を有して構成される。第2開閉弁16は、排水路15の希釈槽30寄りの一端部側に設けられている。 The dilution tank 30 is formed by rotatably arranging a propeller (not shown) in an internal space. The other end of the discharge path 11 is connected to the dilution tank 30. The dilution tank 30 dilutes the mixture M discharged from the mixer 70 via the discharge path 11 with water to generate a diluent T. The dilution tank 30 dilutes the mixture M while rotating a propeller (not shown) in the tank by a motor 30A. The driving of the motor 30A is controlled by the control unit 50. The dilution tank 30 is provided with a third measuring unit 30D that measures the amount of current consumed by the motor 30A that rotates the propeller. Based on the magnitude of the current consumption measured by the third measuring unit 30D, the state of processing in the dilution tank 30 is determined by the determining unit 51. In this case, the third measurement unit 30D functions as an information acquisition unit that acquires the amount of power consumption of the motor 30A as information on the operation state of the dilution tank 30. Specifically, the magnitude of the consumed current measured by the third measuring unit 30D is compared with two predetermined values to determine whether or not the dilution tank 30 is processing the mixture M. The details will be described later in the operation description. The dilution tank 30 is connected to one end of a drainage channel 15 for discharging the generated diluent T to the separation unit 40. The drainage channel 15 is provided with a second on-off valve 16 for opening and closing the drainage channel 15. The opening and closing operation of the second on-off valve 16 is controlled by the control unit 50. The second on-off valve 16 includes, for example, a known electric ball valve or the like, like the first on-off valve 12. The second on-off valve 16 is provided at one end of the drainage channel 15 near the dilution tank 30.
 分離部40は、排水路15の他端が連結されている。分離部40は希釈槽30で生成された希釈物Tをパルプ、プラスティック、ポリマー等の固形分Scと水分Lとに分離する。分離部40は、例えば、公知のスクリュープレス装置等を有して構成される。分離部40はモータ40Cによってスクリュー(図示せず)を回転することによって希釈物Tを分離する。モータ40Cの駆動は制御部50によって制御される。分離部40にはスクリューを回転させるモータ40Cの消費電流の大きさを測定する第4測定部40Fが設けられている。この第4測定部40Fが測定した消費電流の大きさに基づいて、分離部40における処理の状況が判定部51によって判定される。この場合、第4測定部40Fはモータ40Cの消費電力の大きさを分離部40の運転状態に関する情報として取得する情報取得部として機能する。具体的には、第4測定部40Fが測定した消費電流の大きさを所定値と比較して、分離部40が希釈物Tを処理中であるか否かが判定される。詳細は後述の動作説明にて説明する。分離部40には、分離した固形分Scを排出する固形分排出部40Dと、分離した水分Lを排出する下流側排水路15Cとが連結されている。固形分排出部40Dの末端には回収袋40Eが着脱自在に取り付けられて回収される固形分Scが貯留される。下流側排水路15Cは外部の下水道に接続されており、分離した水分Lはそのまま下水として排出される。下流側排水路15Cにはトラップ15Aが設けられている。本実施形態の場合、下流側排水路15Cには図示しない噴出部が設けられており、この噴出部から水を排水方向に噴出することで、トラップ15Aに滞留する水分Lを強制的に排出することができる。 The other end of the drainage path 15 is connected to the separation unit 40. The separation unit 40 separates the diluent T generated in the diluting tank 30 into a solid content Sc such as pulp, plastic, and polymer and water L. The separation unit 40 is configured to include, for example, a known screw press device or the like. The separation unit 40 separates the diluent T by rotating a screw (not shown) by a motor 40C. The driving of the motor 40C is controlled by the control unit 50. The separation unit 40 is provided with a fourth measurement unit 40F that measures the magnitude of current consumption of a motor 40C that rotates the screw. Based on the magnitude of the current consumption measured by the fourth measuring unit 40F, the state of the processing in the separating unit 40 is determined by the determining unit 51. In this case, the fourth measurement unit 40F functions as an information acquisition unit that acquires the amount of power consumption of the motor 40C as information on the operation state of the separation unit 40. Specifically, the magnitude of the current consumption measured by the fourth measurement unit 40F is compared with a predetermined value, and it is determined whether or not the separation unit 40 is processing the dilution T. The details will be described later in the operation description. The separation unit 40 is connected to a solids discharge unit 40D that discharges the separated solids Sc and a downstream drain 15C that discharges the separated water L. A collection bag 40E is detachably attached to the end of the solid content discharge unit 40D to store the collected solid content Sc. The downstream drain 15C is connected to an external sewer, and the separated water L is discharged as it is. A trap 15A is provided in the downstream drainage channel 15C. In the case of the present embodiment, a spout portion (not shown) is provided in the downstream drainage channel 15C, and water is spouted from the spout portion in the drainage direction, thereby forcibly discharging the water L retained in the trap 15A. be able to.
 計測部52は投入部10の投入口に設けられている。本実施形態において、計測部52は光電センサを有して構成されている。計測部52は投入部10に投入された紙おむつDdの個数を計測する。計測部52は通過する紙おむつDdの光電センサによる検知時間に基づいて、紙おむつDdの大きさ、例えば、大便用紙おむつと小便用紙おむつとの大きさの差異を判別しつつ個数を計測することができるように構成されている。計測部52による計測結果は制御部50に送られる。計測部によって計測されるものとしては、被処理物の個数や大きさのみならず、被処理物の重量等であってもよい。 The measuring unit 52 is provided at the input port of the input unit 10. In the present embodiment, the measurement unit 52 is configured to include a photoelectric sensor. The measuring unit 52 measures the number of the disposable diapers Dd supplied to the input unit 10. The measuring unit 52 can measure the number of disposable diapers Dd while determining the size of the disposable diapers Dd based on the detection time of the passing diapers Dd by the photoelectric sensor, for example, the difference between the stool diapers and the urine diapers. It is configured as follows. The measurement result by the measurement unit 52 is sent to the control unit 50. What is measured by the measuring unit may be not only the number and size of the objects to be processed, but also the weight of the objects to be processed.
 制御部50は装置各部の制御を行う。具体的には、本実施形態において、制御部50は処理剤投入部23の各部23A,23Bの制御、処理部90の各モータ20G,70A,30A,40Cの駆動制御、電磁弁14E、第1開閉弁12、及び第2開閉弁16の開閉制御を行う。本実施形態では、制御部50は判定部51によって、計測部52の計測結果に基づいて紙おむつDdの状態の判定を行う。判定部51は第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fの測定結果に基づいた紙おむつDdの状態の判定も行う。具体的には、判定部51は処理部90の破砕部20、ミキサ70、希釈槽30、及び分離部40の各部について、第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fの各測定部によって測定されたモータ20G,70A,30A,40Cの消費電流値に基づいた紙おむつDdの状態の判定を行う。 The control unit 50 controls each unit of the apparatus. Specifically, in the present embodiment, the control unit 50 controls the respective units 23A and 23B of the processing agent input unit 23, the drive control of the motors 20G, 70A, 30A and 40C of the processing unit 90, the electromagnetic valve 14E, the first Open / close control of the on-off valve 12 and the second on-off valve 16 is performed. In the present embodiment, the control unit 50 causes the determination unit 51 to determine the state of the paper diaper Dd based on the measurement result of the measurement unit 52. The determination unit 51 also determines the state of the paper diaper Dd based on the measurement results of the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F. Specifically, the determination unit 51 determines the first measuring unit 20H, the second measuring unit 70B, the third measuring unit 30D, and the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40 of the processing unit 90. Then, the state of the disposable diaper Dd is determined based on the current consumption values of the motors 20G, 70A, 30A, 40C measured by the measuring units of the fourth measuring unit 40F.
 本実施形態において、制御部50は処理部90の運転状態に関する情報を取得する情報取得部として機能する。具体的には、制御部50は処理部の運転状態に関する情報として処理部90の各部(破砕部20、ミキサ70、希釈槽30、及び分離部40)の負荷軽減時間を取得する。処理部90の負荷低減時間とは、処理部90の各部において、処理を開始して一旦上昇した各モータ20G,70A,30A,40Cの消費電流値が所定値以下に低下するまでの時間である。すなわち、制御部50は第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fが測定した各モータ20G,70A,30A,40Cの消費電流の変動に基づいて、処理部90の運転状態に関する情報としての負荷低減時間を取得する。 In the present embodiment, the control unit 50 functions as an information acquisition unit that acquires information on the operation state of the processing unit 90. Specifically, the control unit 50 acquires the load reduction time of each unit (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) of the processing unit 90 as information on the operation state of the processing unit. The load reduction time of the processing unit 90 is a time until the current consumption of each of the motors 20G, 70A, 30A, and 40C, which has been increased after the processing is started, is reduced to a predetermined value or less in each unit of the processing unit 90. . That is, the control unit 50 controls the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F based on the fluctuations in the current consumption of the motors 20G, 70A, 30A, and 40C. , The load reduction time as information on the operation state of the processing unit 90 is acquired.
 本実施形態において、判定部51は処理部90の運転状態に関する情報として制御部50が取得した負荷軽減時間に基づいて、処理部90の各部(破砕部20、ミキサ70、希釈槽30、及び分離部40)の状況を判定する。判定部51は、例えば、処理部90の運転状態に関する情報として第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fが測定した測定結果である各モータ20G,70A,30A,40Cの消費電流値に基づいて、処理部90の各部(破砕部20、ミキサ70、希釈槽30、及び分離部40)の状況を判定することもできる。この場合、第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fは処理部90の運転状態に関する情報としての消費電力値を取得する情報取得部として機能する。 In the present embodiment, based on the load reduction time acquired by the control unit 50 as the information on the operation state of the processing unit 90, the determination unit 51 determines each part of the processing unit 90 (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit). The status of the unit 40) is determined. For example, the determination unit 51 determines each motor 20G as a measurement result measured by the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F as information on the operation state of the processing unit 90. , 70A, 30A, and 40C, the status of each unit (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) of the processing unit 90 can be determined. In this case, the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F function as an information acquisition unit that acquires a power consumption value as information regarding the operation state of the processing unit 90. .
 本実施形態に係る報知部53は汚物処理装置6の稼働状況に関する情報を文字や図形で表示する表示器である。報知部53は、例えば、図6に示すように、投入部10の投入口の外部等に配置される。報知部53によって報知される稼働状況に関する情報としては、例えば、被処理物である紙おむつDdの状態やそれに関する情報(例えば、計測部52によって計測された紙おむつDdの個数、紙おむつDdの重量)、処理部90の各部(破砕部20、ミキサ70、希釈槽30、及び分離部40)の運転状態やそれらに関する情報(例えば、第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fによる測定値)、処理部90の各部(破砕部20、ミキサ70、希釈槽30、及び分離部40)の状況(例えば、現在行っている処理工程、紙おむつDdの処理の開始から現在までの時間、現在から処理終了までの想定時間、現在から次に紙おむつDdを投入可能になるまでの想定時間等)、処理剤投入部23に貯留されている処理剤の残量、異常の発生の有無、発生した異常の内容等が挙げられる。 The notification unit 53 according to the present embodiment is a display that displays information about the operation status of the waste disposal apparatus 6 in characters or graphics. The notification unit 53 is arranged, for example, outside the input port of the input unit 10, as shown in FIG. Examples of the information on the operating status notified by the notifying unit 53 include the state of the disposable diaper Dd as an object to be processed and information related thereto (for example, the number of disposable diapers Dd measured by the measuring unit 52, the weight of the disposable diaper Dd), The operating state of each part (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) of the processing unit 90 and information related thereto (for example, the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, And the state of each unit (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) of the processing unit 90 (for example, the current processing step, the processing of the disposable diaper Dd). The time from the start to the present, the expected time from the present to the end of the process, the expected time from the present to the next disposable diaper Dd, etc.) And that the remaining amount of the treatment agent, the presence or absence of abnormality occurrence, contents, etc., of the abnormality that has occurred, and the like.
 本実施形態に係る記憶部54は報知部53によって報知される稼働状況に関する情報として挙げた情報のデータ等を記憶する。記憶部54はこれらの情報のデータや装置の制御プログラム等を格納可能な記憶媒体である。記憶部54は計測部52の計測結果、処理剤投入部23からの処理剤の投入量、第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fが測定する測定値やこれらに基づいて制御部50が取得する後述する負荷低減時間、判定部51の判定結果等の汚物処理装置6の稼働中に取得した各種の情報を汚物処理装置6の稼働状況に関する情報として記憶する。 (4) The storage unit 54 according to the present embodiment stores data of information listed as information on the operation status notified by the notification unit 53 and the like. The storage unit 54 is a storage medium capable of storing such information data and a control program for the apparatus. The storage unit 54 measures the measurement result of the measurement unit 52, the amount of the treatment agent supplied from the treatment agent introduction unit 23, and the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F. Various information acquired during the operation of the waste disposal apparatus 6 such as a measured value to be performed, a load reduction time acquired by the control unit 50 based on the measured values, and a determination result of the determination unit 51 are related to the operation status of the waste disposal apparatus 6. Store as information.
 本実施形態に係る送信部55は報知部53によって報知される稼働状況に関する情報として挙げた情報のデータ等を送信する。送信部55は、例えば、公知の通信機器等を有して構成される。送信部55から送信された情報は管理センターの管理機器や携帯端末等の外部の受信部によって受信し得る。 送信 The transmitting unit 55 according to the present embodiment transmits data of information listed as information on the operating status notified by the notifying unit 53 and the like. The transmission unit 55 includes, for example, a known communication device or the like. The information transmitted from the transmitting unit 55 can be received by an external receiving unit such as a management device of a management center or a portable terminal.
 次に、第4及び第5の汚物処理装置6の動作について説明する。
 最初に、投入部10の第1蓋60を開け、使用済みの紙おむつDdを投入部10に投入する(投入工程)。投入部10から紙おむつDdが投入されると、制御部50は破砕部20及びミキサ70の運転を開始するとともに排出路11の第1開閉弁12を閉じる制御を実行する。これによって紙おむつDdの処理が開始される。投入部10から紙おむつDdが投入されると、計測部52は投入された紙おむつDdの個数を計測する。更に本実施形態の場合、光電センサである計測部52は1つの紙おむつDd毎の検知している時間を計測する。これに基づいて、制御部50は紙おむつDdの大きさを推定する。具体的には、制御部50は計測部52によって計測された紙おむつDdの検知時間の長短に応じて、大便用の紙おむつであるか、小便用の紙おむつであるかを推測し、例えば、大便用の紙おむつを1個とした場合には小便用の紙おむつを0.5個とする等の方法で、紙おむつの種類による重みづけをする。制御部50は計測部52が計測した計測結果である紙おむつDdの個数に基づいて投入された紙おむつDdの状態を判定し、処理剤の投入量を決定する。制御部50は決定した投入量の処理剤を処理剤投入部23から投入させる(処理剤投入工程)。本実施形態の場合、通常運転における処理剤投入工程では、酢酸カルシウムを含む処理剤及び塩化カルシウムを含む処理剤が第1処理剤投入部23A及び第2処理剤投入部23Bのそれぞれから投入される。制御部50は、電磁弁14Eの開閉制御を実行し、計測部52が計測した紙おむつDdの投入量に応じた水を吐出部14から供給する。
Next, the operation of the fourth and fifth waste disposal apparatuses 6 will be described.
First, the first lid 60 of the input unit 10 is opened, and the used paper diaper Dd is input into the input unit 10 (input step). When the disposable diaper Dd is inserted from the input unit 10, the control unit 50 starts the operation of the crushing unit 20 and the mixer 70 and executes control to close the first on-off valve 12 of the discharge path 11. Thus, the processing of the disposable diaper Dd is started. When the disposable diapers Dd are inserted from the input unit 10, the measuring unit 52 counts the number of the disposable diapers Dd. Furthermore, in the case of the present embodiment, the measuring unit 52, which is a photoelectric sensor, measures the detection time for each paper diaper Dd. Based on this, the control unit 50 estimates the size of the paper diaper Dd. Specifically, the control unit 50 estimates whether the diaper is a stool diaper or a urine diaper in accordance with the length of the detection time of the diaper Dd measured by the measurement unit 52. When one disposable diaper is used, weighting is performed according to the type of disposable diaper, for example, by using 0.5 urinal disposable diapers. The control unit 50 determines the state of the disposable diapers Dd based on the number of disposable diapers Dd, which is the measurement result measured by the measuring unit 52, and determines the amount of the treatment agent to be introduced. The control unit 50 causes the processing agent input unit 23 to input the determined input amount of the processing agent (processing agent input step). In the case of the present embodiment, in the processing agent charging step in the normal operation, the processing agent including calcium acetate and the processing agent including calcium chloride are supplied from each of the first processing agent input section 23A and the second processing agent input section 23B. . The control unit 50 executes opening / closing control of the electromagnetic valve 14E, and supplies water according to the amount of the disposable diaper Dd measured by the measuring unit 52 from the discharge unit 14.
 処理剤投入工程において、制御部50は決定した投入量に対して、処理剤投入部23から投入可能な処理剤の量の不足を検出したときには、処理部90の運転を停止する制御を実行する。本実施形態の場合、制御部50は投入された紙おむつDdの個数に応じた処理剤の量に対しての残量の不足を検出した場合に、処理部90の各部を停止して処理を中止する。制御部50は処理剤の残量不足を報知部53に報知させる。このとき、例えば、制御部50は処理剤投入部23への処理剤の補充が確認された場合や、手動によって投入部10の投入口から処理剤が投入されたことを確認した場合等、処理を正常に実行可能な状態になったことが確認できた場合には、処理部90の運転を自動的に再開する制御を実行してもよい。 In the processing agent supply step, when the control unit 50 detects that the amount of the processing agent that can be supplied from the processing agent supply unit 23 is insufficient with respect to the determined supply amount, the control unit 50 executes control to stop the operation of the processing unit 90. . In the case of the present embodiment, when the control unit 50 detects the shortage of the remaining amount with respect to the amount of the processing agent according to the number of the disposable diapers Dd, the control unit 50 stops each unit of the processing unit 90 and stops the processing. I do. The control unit 50 causes the notification unit 53 to notify the shortage of the remaining amount of the processing agent. At this time, for example, when the control unit 50 confirms replenishment of the processing agent into the processing agent input unit 23, or when it is confirmed that the processing agent is manually input from the input port of the input unit 10, the control unit 50 performs processing. If it can be confirmed that the state has become normally executable, the control of automatically restarting the operation of the processing unit 90 may be executed.
 投入部10から投入された紙おむつDdは破砕部20に落下して破砕処理される(破砕工程)。破砕部20では吐出部14から供給された水とともに紙おむつDdを破砕する。このとき、制御部50は処理部の運転状態に関する情報としてのモータ20Gの消費電流の大きさを第1測定部20Hによって測定する。測定した消費電流値は記憶部54に記憶される。制御部50は消費電流の大きさが所定の大きさ以下になるまでモータ20Gを駆動制御して回転刃を回転させ続ける。破砕工程では紙おむつDdが細かく破砕されることによって破砕物Cとされて下方のシュート21に徐々に落下するため、破砕が進むにつれてモータ20Gの負荷が徐々に小さくなる。制御部50はこの第1測定部20Hが測定する値の変動を監視して、破砕部20がどのような状況にあるのかを判定部51によって判定する。 (4) The disposable diaper Dd supplied from the input unit 10 falls into the crushing unit 20 and is crushed (crushing step). The crushing unit 20 crushes the paper diaper Dd together with the water supplied from the discharge unit 14. At this time, the control unit 50 measures the magnitude of the current consumption of the motor 20G as information on the operation state of the processing unit by the first measurement unit 20H. The measured current consumption value is stored in the storage unit 54. The control unit 50 continues to rotate the rotary blade by controlling the drive of the motor 20G until the amount of current consumption becomes equal to or less than a predetermined value. In the crushing step, the disposable diaper Dd is finely crushed to be crushed material C and gradually falls to the lower chute 21, so that as the crushing proceeds, the load on the motor 20G gradually decreases. The control unit 50 monitors the change of the value measured by the first measurement unit 20H, and determines the state of the crushing unit 20 by the determination unit 51.
 判定部51は第1測定部20Hが測定したモータ20Gの消費電流の大きさが所定値以下である場合には、破砕部20の状況が「無負荷(空運転)」であると判定する。判定部51は第1測定部20Hが測定したモータ20Gの消費電流の大きさが所定値以下でない場合には、破砕部20の状況として「破砕中」であると判定する。判定部51は破砕部20の状況が「破砕中」から所定時間内に「無負荷」となった場合には、「破砕処理済み」の状況であると判定する。この場合、制御部50は破砕部20の運転を停止させるとともにミキサ70の運転を開始させる。この時、制御部50は、破砕部20における処理時間を計測し、この計測結果に応じた処理剤の追加投入量を決定する。具体的には、制御部50は、破砕部20の状況が「破砕中」であった時間に基づいて、紙おむつDdの個数を推定するとともに、計測部52にて計測した紙おむつDdの個数と比較する。制御部50は推定した紙おむつDdの個数が計測部52の計測結果よりも大きい場合には、その差に応じた処理剤の追加投入量を決定して処理剤投入部23から追加で投入させる。一方、制御部50は推定した紙おむつDdの個数が計測部52の計測結果よりも小さい場合には、追加投入量を0と決定する。すなわちこの場合、制御部50は処理剤を追加して投入しない。 (4) When the magnitude of the current consumption of the motor 20G measured by the first measuring unit 20H is equal to or smaller than a predetermined value, the determining unit 51 determines that the state of the crushing unit 20 is “no load (idle operation)”. When the magnitude of the current consumption of the motor 20G measured by the first measuring unit 20H is not smaller than or equal to the predetermined value, the determining unit 51 determines that the state of the crushing unit 20 is “crushing”. When the state of the crushing unit 20 becomes “no load” within a predetermined time from “under crushing”, the determination unit 51 determines that the state is “crushed”. In this case, the control unit 50 stops the operation of the crushing unit 20 and starts the operation of the mixer 70. At this time, the control unit 50 measures the processing time in the crushing unit 20, and determines an additional amount of the processing agent to be added according to the measurement result. Specifically, the control unit 50 estimates the number of the disposable diapers Dd based on the time when the state of the crushing unit 20 is “under crushing”, and compares the estimated number with the number of the disposable diapers Dd measured by the measuring unit 52. I do. When the estimated number of disposable diapers Dd is larger than the measurement result of the measuring unit 52, the control unit 50 determines an additional amount of the processing agent according to the difference, and causes the processing agent input unit 23 to additionally input the amount. On the other hand, when the estimated number of the disposable diapers Dd is smaller than the measurement result of the measurement unit 52, the control unit 50 determines the additional amount to be 0. That is, in this case, the control unit 50 does not add the processing agent.
 シュート21を経由して破砕部20から落下した破砕物Cは、ミキサ70にて混合処理される(混合工程)。混合処理では、ミキサ70において、破砕物Cと、吐出部14から供給された水分と、処理剤投入部23から投入された処理剤とを混合する。これによって、水分を吸収したポリマーと処理剤とが反応して、ポリマーを含む紙おむつDdの固形成分と、ポリマーから不可逆的に分離された水分と、が混合された混合物Mが生成される。このとき、制御部50は、処理部の運転状態に関する情報として、モータ70Aの消費電流の大きさを第2測定部70Bによって測定する。測定した消費電流値は記憶部54に記憶される。制御部50は、消費電流の大きさが所定の大きさ以下になるまでモータ70Aを駆動制御して回転刃(図示せず)を回転させ続ける。混合工程では、ポリマーと処理剤との反応が進むにしたがって水分が分離されて混合物Mの粘度が小さくなるため、モータ70Aの負荷が徐々に小さくなる。制御部50は、この第2測定部70Bが測定する値の変動を監視して、判定部51によってミキサ70がどのような状況にあるのかを判定する。 (4) The crushed material C dropped from the crushing unit 20 via the chute 21 is mixed by the mixer 70 (mixing step). In the mixing process, the crushed material C, the water supplied from the discharge unit 14, and the processing agent input from the processing agent input unit 23 are mixed in the mixer 70. As a result, the polymer that has absorbed the water and the treating agent react with each other to generate a mixture M in which the solid component of the disposable diaper Dd containing the polymer and the water irreversibly separated from the polymer are mixed. At this time, the control unit 50 measures the magnitude of the current consumption of the motor 70A by the second measuring unit 70B as information on the operation state of the processing unit. The measured current consumption value is stored in the storage unit 54. The control unit 50 controls the drive of the motor 70A and keeps rotating the rotary blade (not shown) until the magnitude of the current consumption becomes equal to or smaller than the predetermined magnitude. In the mixing step, as the reaction between the polymer and the treatment agent progresses, the water is separated and the viscosity of the mixture M decreases, so that the load on the motor 70A gradually decreases. The control unit 50 monitors the change of the value measured by the second measurement unit 70B, and determines the state of the mixer 70 by the determination unit 51.
 ミキサ70のモータ70Aの消費電流は、図8に示すように、混合工程を実行してしばらくの間、値Aが維持され、その後、値Aから徐々に小さくなり値Bに到達し、値Bが維持される。ミキサ70で破砕物Cと処理剤とを混合開始した直後には、ミキサ70のモータ70Aの消費電流は値Aを示す。モータ70Aの消費電流はポリマーと処理剤との反応が進行するにつれて値Aから徐々に小さくなる。ポリマーと処理剤との反応がほぼ終了すると、ミキサ70のモータ70Aの消費電流は値Aよりも小さい値Bを示す。 As shown in FIG. 8, the current consumption of the motor 70A of the mixer 70 is maintained at the value A for a while after executing the mixing process, and thereafter gradually decreases from the value A to reach the value B. Is maintained. Immediately after the start of mixing the crushed material C and the treatment agent in the mixer 70, the current consumption of the motor 70A of the mixer 70 indicates the value A. The current consumption of the motor 70A gradually decreases from the value A as the reaction between the polymer and the treatment agent progresses. When the reaction between the polymer and the treating agent is almost completed, the current consumption of the motor 70A of the mixer 70 shows a value B smaller than the value A.
 判定部51は第2測定部70Bが測定したモータ70Aの消費電流の大きさが第1の所定値以下である場合には、ミキサ70の状況が「無負荷(空運転)」であると判定する。この第1の所定値は図8における値Bよりも小さい値として設定されている。第2測定部70Bが測定したモータ70Aの消費電流の大きさが第2の所定値以上である場合、判定部51は、ミキサ70の状況がポリマーと処理剤とを反応させる処理の途中である「ポリマー処理中」であると判定する。この第2の所定値は図8における値Aよりも小さく且つ値Bよりも大きな値として設定されている。ミキサ70の状況が「ポリマー処理中」である状態から、所定時間内に、第2測定部70Bが測定したモータ70Aの消費電流の大きさが第2の所定値以上でない状態になった場合、判定部51はミキサ70の状況として「ポリマー処理済み」であると判定する。この場合、制御部50は、排水路15の第2開閉弁16を閉塞するとともに排出路11の第1開閉弁12を開放し、混合物Mを希釈槽30に導入させる。このとき、制御部50は希釈槽30の運転も開始させる。 If the magnitude of the current consumption of the motor 70A measured by the second measuring unit 70B is equal to or smaller than the first predetermined value, the determining unit 51 determines that the state of the mixer 70 is “no load (idle operation)”. I do. This first predetermined value is set as a value smaller than the value B in FIG. When the magnitude of the current consumption of the motor 70A measured by the second measuring unit 70B is equal to or larger than the second predetermined value, the determining unit 51 determines that the state of the mixer 70 is in the process of causing the polymer to react with the treating agent. It is determined that "polymer processing is in progress". This second predetermined value is set as a value smaller than the value A and larger than the value B in FIG. When the current consumption of the motor 70A measured by the second measuring unit 70B is not greater than or equal to the second predetermined value within a predetermined time from the state where the mixer 70 is in the “polymer processing” state, The determination unit 51 determines that the state of the mixer 70 is “polymer processed”. In this case, the control unit 50 closes the second on-off valve 16 of the drain passage 15 and opens the first on-off valve 12 of the discharge passage 11 to introduce the mixture M into the dilution tank 30. At this time, the control unit 50 also starts the operation of the dilution tank 30.
 ミキサ70から排出された混合物Mは排出路11を経由して希釈槽30に導入されて希釈処理される(希釈工程)。希釈処理では、希釈槽30において、混合物Mと水とを撹拌することによって混合物Mを希釈する。希釈工程において、混合物Mは混合物Mに含まれる処理剤成分の濃度が所定値以下(例えば、塩素濃度が300ppm以下)になるように希釈される。これによって、混合物Mが下水に排出可能な濃度に希釈された希釈物Tを生成される。このとき、判定部51は計測部52にて計測した紙おむつDdの個数、及び第1測定部20Hの測定結果の少なくともいずれか一方に基づいて制御部50が推定した紙おむつDdの個数に基づいて被処理物としての紙おむつDdの状態を判定し、制御部50は判定部51の判定結果に基づいてこれに応じた所定の量の水を吐出部14から供給させる。これによって、破砕部20、シュート21、ミキサ70、排出路11を洗浄しつつ、希釈槽30に水が供給される。処理剤としての酢酸カルシウムはCl(塩素)分を含まないため、従来のように塩化カルシウムのみを処理剤として用いた場合と比較して、希釈する水量を減らすことができる。 The mixture M discharged from the mixer 70 is introduced into the dilution tank 30 via the discharge path 11 and is diluted (dilution process). In the dilution process, the mixture M is diluted by stirring the mixture M and water in the dilution tank 30. In the dilution step, the mixture M is diluted such that the concentration of the treating agent component contained in the mixture M becomes a predetermined value or less (for example, the chlorine concentration is 300 ppm or less). As a result, a dilution T in which the mixture M is diluted to a concentration that can be discharged to the sewage is generated. At this time, the determination unit 51 determines the number of the paper diapers Dd measured by the measurement unit 52 and the number of the paper diapers Dd estimated by the control unit 50 based on at least one of the measurement results of the first measurement unit 20H. The state of the paper diaper Dd as a processing object is determined, and the control unit 50 supplies a predetermined amount of water from the discharge unit 14 according to the determination result of the determination unit 51. Thereby, water is supplied to the dilution tank 30 while washing the crushing unit 20, the chute 21, the mixer 70, and the discharge path 11. Since calcium acetate as a treating agent does not contain Cl (chlorine), the amount of water to be diluted can be reduced as compared with the case where only calcium chloride is used as a treating agent as in the related art.
 希釈工程において、制御部50は、処理部の運転状態に関する情報として、モータ30Aの消費電流の大きさを第3測定部30Dによって測定する。測定した消費電流値は記憶部54に記憶される。制御部50は、消費電流の大きさが所定の大きさ以下になるまでモータ30Aを駆動制御してプロペラ(図示せず)を回転させ続ける。希釈工程では、混合物Mの水分割合が増加するにしたがって粘度が小さくなるため、モータ30Aの負荷が徐々に小さくなる。制御部50は、この第3測定部30Dが測定する値の変動を監視して、判定部51によって希釈槽30がどのような状況にあるのかを判定する。 In the dilution step, the control unit 50 measures the magnitude of the current consumption of the motor 30A by the third measurement unit 30D as information on the operation state of the processing unit. The measured current consumption value is stored in the storage unit 54. The control unit 50 controls the driving of the motor 30A and keeps rotating the propeller (not shown) until the amount of current consumption becomes equal to or smaller than a predetermined value. In the dilution step, the viscosity decreases as the water content of the mixture M increases, so that the load on the motor 30A gradually decreases. The control unit 50 monitors the fluctuation of the value measured by the third measurement unit 30D, and determines the state of the dilution tank 30 by the determination unit 51.
 判定部51は第3測定部30Dが測定したモータ30Aの消費電流の大きさが第1の所定値以下である場合には、希釈槽30の状況が「無負荷(空運転)」であると判定する。判定部51は第3測定部30Dが測定したモータ30Aの消費電流の大きさが第2の所定値以上の場合には、希釈槽30の状況が「希釈処理中」であると判定する。この第2の所定値は、第1の所定値よりも大きな値として設定されている。希釈槽30の状況が「希釈処理中」である状態から、所定時間内に、第3測定部30Dが測定したモータ30Aの消費電流の大きさが第2の所定値以上でない状態になった場合、判定部51は希釈槽30の状況として「希釈処理済み」であると判定する。この場合、制御部50は排水路15の第2開閉弁16を開放して希釈物Tを希釈槽30から排出させるとともに分離部40の運転を開始させる。 When the magnitude of the current consumption of the motor 30A measured by the third measuring unit 30D is equal to or smaller than the first predetermined value, the determining unit 51 determines that the state of the dilution tank 30 is “no load (idle operation)”. judge. When the magnitude of the current consumption of the motor 30A measured by the third measurement unit 30D is equal to or larger than the second predetermined value, the determination unit 51 determines that the state of the dilution tank 30 is “dilution process”. This second predetermined value is set as a value larger than the first predetermined value. When the magnitude of the current consumption of the motor 30A measured by the third measuring unit 30D does not exceed the second predetermined value within a predetermined time from the state of the dilution tank 30 being “dilution processing” The determination unit 51 determines that the state of the dilution tank 30 is “diluted”. In this case, the control unit 50 opens the second on-off valve 16 of the drainage channel 15 to discharge the diluent T from the dilution tank 30 and starts the operation of the separation unit 40.
 希釈槽30から排出された希釈物Tは排水路15を経由して分離部40に導入されて分離処理される(分離工程)。分離処理では分離部40において、希釈物Tを固形分Scと水分Lとに分離する。分離部40において分離された固形分Scは固形分排出部40Dを経由して回収袋40Eに貯留される。分離部40において分離された水分Lは下流側排水路15Cから排出され、トラップ15Aを経由して外部の下水道に排出される。トラップ15Aには、分離部40において分離されることなく下流側排水路15Cに排出された固形分Scが滞留するおそれがあるため、制御部50の制御によって噴出部(図示せず)から水を定期的に噴出させて強制的に排出させる。 (4) The diluent T discharged from the dilution tank 30 is introduced into the separation unit 40 via the drainage channel 15 and is separated (separation step). In the separation process, the diluent T is separated into the solid content Sc and the water L in the separation unit 40. The solid content Sc separated in the separation unit 40 is stored in the collection bag 40E via the solid content discharge unit 40D. The water L separated in the separation section 40 is discharged from the downstream drainage channel 15C, and discharged to the external sewer through the trap 15A. In the trap 15A, there is a possibility that the solid content Sc discharged to the downstream drainage channel 15C without being separated in the separation unit 40 may stay. Eject periodically to force discharge.
 分離工程において、制御部50は処理部の運転状態に関する情報として、モータ40Cの消費電流の大きさを第4測定部40Fによって測定する。測定した消費電流値は記憶部54に記憶される。制御部50は消費電流の大きさが所定の大きさ以下になるまでモータ40Cを駆動制御してスクリューを回転させ続ける。分離工程では、希釈物Tからの固形分Scと水分Lの分離が進行するにしたがってモータ40Cの負荷が徐々に小さくなる。制御部50は、この第4測定部40Fが測定する値の変動を監視して、判定部51によって分離部40がどのような状況にあるのかを判定する。 In the separation step, the control unit 50 measures the magnitude of the current consumption of the motor 40C by the fourth measurement unit 40F as information on the operation state of the processing unit. The measured current consumption value is stored in the storage unit 54. The control unit 50 continues to rotate the screw by controlling the drive of the motor 40C until the amount of current consumption becomes equal to or less than a predetermined amount. In the separation step, the load on the motor 40C gradually decreases as the separation of the solid content Sc and the water L from the diluent T progresses. The control unit 50 monitors the change of the value measured by the fourth measurement unit 40F, and determines the state of the separation unit 40 by the determination unit 51.
 判定部51は第4測定部40Fが測定したモータ40Cの消費電流の大きさが所定値以下である場合には、分離部40の状況が「無負荷(空運転)」であると判定する。判定部51は第4測定部40Fが測定したモータ40Cの消費電流の大きさが所定値以上の場合には、分離部40の状況が「分離処理中」であると判定する。分離部40の状況が「分離処理中」である状態から、所定時間内に、「無負荷」である状態になった場合、判定部51は分離部40の状況として「分離処理済み」であると判定する。この場合、制御部50は分離部40の運転を停止させる。これによって紙おむつDdの処理が完了する。 (4) If the magnitude of the current consumption of the motor 40C measured by the fourth measuring unit 40F is equal to or smaller than a predetermined value, the determining unit 51 determines that the state of the separating unit 40 is “no load (idle operation)”. When the magnitude of the current consumption of the motor 40C measured by the fourth measuring unit 40F is equal to or larger than a predetermined value, the determining unit 51 determines that the state of the separating unit 40 is “separating”. When the status of the separation unit 40 changes from “state of separation processing” to “no load” within a predetermined time, the determination unit 51 determines that the state of the separation unit 40 is “separation processing completed”. Is determined. In this case, the control unit 50 stops the operation of the separation unit 40. Thus, the processing of the disposable diaper Dd is completed.
 次に、汚物処理装置6において異常が発生した際の是正方法について説明する。破砕工程において異常が発生した場合、例えば、破砕工程において、紙おむつDdが投入されたにも関わらず、破砕部20において「無負荷」の状況から所定時間経過しても変化がない場合には、判定部51は異常が発生したと判定する。具体的には、破砕部20の上流側となる投入部10内において紙おむつDdの詰まりが発生した可能性が考えられる。この場合、判定部51は破砕工程において「詰まり」の異常が発生したと判定する。この場合には、制御部50は破砕部20の運転を停止し、破砕工程にて異常が発生したことを報知部53によって報知させる。この場合には、作業者によって、第1蓋60を開けて投入部10内を確認し、紙おむつDdの詰まりを解消する。その後、破砕部20の運転を再開する。 Next, a method for correcting an abnormality in the waste disposal apparatus 6 will be described. When an abnormality occurs in the crushing step, for example, in the crushing step, in spite of the disposable diaper Dd being input, if there is no change in the crushing unit 20 from the “no load” state for a predetermined time, The determination unit 51 determines that an abnormality has occurred. Specifically, it is conceivable that the paper diaper Dd may be jammed in the charging section 10 on the upstream side of the crushing section 20. In this case, the determination unit 51 determines that an abnormality of “clogging” has occurred in the crushing process. In this case, the control unit 50 stops the operation of the crushing unit 20 and causes the notification unit 53 to notify that an abnormality has occurred in the crushing process. In this case, the operator opens the first lid 60 and checks the inside of the input unit 10 to eliminate the jam of the paper diaper Dd. Thereafter, the operation of the crushing unit 20 is restarted.
 破砕工程において、「破砕中」の状況が紙おむつDdの投入後に所定時間経過しても変化がない場合、判定部51は紙おむつDdの投入過多や汚れの蓄積が発生したと判定(「過負荷」と判定)する。この場合、制御部50は破砕部20の運転を停止し、報知部53に報知させる。この場合には、作業者は第1蓋60を開けて投入部10内の紙おむつDdの投入量を確認する。紙おむつDdの投入過多を確認した場合にはいくつかの紙おむつDdを取り出す。一方、投入部10内の紙おむつDdの個数が通常の個数以下であることを確認した場合には汚れの蓄積が想定される。この場合には破砕部20の洗浄モードを実行する。すなわち、破砕部20の洗浄モードは作業者によって異常状態が確認されたのち、作業者が操作ボタンを操作するなどして開始される。 In the crushing process, if the state of “under crushing” does not change even after a predetermined time has passed after the disposable diaper Dd is input, the determination unit 51 determines that excessive input of the disposable diaper Dd or accumulation of dirt has occurred (“overload”). Is determined). In this case, the control unit 50 stops the operation of the crushing unit 20 and causes the notifying unit 53 to notify. In this case, the operator opens the first lid 60 and checks the amount of the disposable diaper Dd in the dispensing section 10. When it is confirmed that the disposable diapers Dd are excessively loaded, some disposable diapers Dd are taken out. On the other hand, when it is confirmed that the number of the disposable diapers Dd in the input unit 10 is equal to or less than the normal number, accumulation of dirt is assumed. In this case, the washing mode of the crushing unit 20 is executed. That is, the washing mode of the crushing unit 20 is started by an operator operating an operation button after an abnormal state is confirmed by the operator.
 作業者による操作ボタンの操作によって破砕部20の洗浄モードが開始されると、制御部50は、最初に、破砕部20の運転を停止させた状態で、破砕工程の次工程である混合工程を完了させ、ミキサ70を空にする。次に、制御部50は吐出部14から水を供給させつつモータ20Gの正転及び逆転駆動を繰り返す制御を実行する。その後、制御部50は、破砕部20が「無負荷」の状態になるまで、すなわち、第1測定部20Hが測定したモータ20Gの消費電流の大きさが所定値よりも小さくなるまでモータ20Gを正転駆動させる。破砕部20の洗浄モードの実行中には、制御部50は破砕部20の洗浄モードを実行中であることを報知部53に報知させる。破砕部20のみならず、以下に説明する処理部90の各部の洗浄モードは湯を使用して行うことが好ましい。水のみを用いた洗浄よりも蓄積した汚れを落としやすいからである。破砕部20の洗浄モードでは、例えば、処理剤である酢酸カルシウムを投入部10から手動で投入するようにしてもよい。この場合、酢酸カルシウムは、固体であってもよいし、水溶液であってもよい。紙おむつDdに含まれる粘着剤の成分が付着している場合、追加で投入した酢酸カルシウムの作用によって剥がれ易くなって好適である。 When the washing mode of the crushing unit 20 is started by the operation of the operation button by the operator, the control unit 50 first stops the operation of the crushing unit 20 and performs the mixing process which is the next process of the crushing process. Upon completion, the mixer 70 is emptied. Next, the control unit 50 executes a control of repeating the forward rotation and the reverse rotation drive of the motor 20G while supplying water from the discharge unit 14. Thereafter, the control unit 50 controls the motor 20G until the crushing unit 20 enters the “no load” state, that is, until the current consumption of the motor 20G measured by the first measuring unit 20H becomes smaller than a predetermined value. Drive forward. While the crushing unit 20 is executing the cleaning mode, the control unit 50 notifies the notification unit 53 that the crushing unit 20 is executing the cleaning mode. It is preferable that the washing mode of not only the crushing unit 20 but also each unit of the processing unit 90 described below is performed using hot water. This is because accumulated dirt is easier to remove than washing using only water. In the cleaning mode of the crushing unit 20, for example, calcium acetate as a treatment agent may be manually input from the input unit 10. In this case, the calcium acetate may be a solid or an aqueous solution. When the component of the pressure-sensitive adhesive contained in the disposable diaper Dd is attached, it is preferable because it is easily peeled off by the action of calcium acetate added additionally.
 混合工程において異常が発生した場合、例えば、ミキサ70の運転が開始されたにも関わらず「無負荷」の状況が所定時間経過しても変化がない場合には、判定部51は異常が発生したと判定する。具体的には、ミキサ70の上流側であるシュート21において破砕物Cの詰まりが発生した可能性が考えられる。この場合、判定部51は混合工程において「詰まり」の異常が発生したと判定する。この場合、制御部50は、吐出部14から水を供給しつつ破砕部20を運転し、シュート21に詰まった破砕物Cをミキサ70に落下させる。その後、制御部50は、ミキサ70の異常状態が解消されたことを確認したら、ミキサ70の通常の運転を再開する。一方、ミキサ70の異常状態が解消されなかった場合には、制御部50は、混合工程において異常が発生したことを報知部53によって報知させ、汚物処理装置6全体を停止させる。 If an abnormality occurs in the mixing process, for example, if the state of “no load” does not change even after a predetermined time has elapsed even though the operation of the mixer 70 has been started, the determination unit 51 generates an abnormality. It is determined that it has been performed. Specifically, it is conceivable that clogging of the crushed material C has occurred in the chute 21 on the upstream side of the mixer 70. In this case, the determination unit 51 determines that an abnormality of “clogging” has occurred in the mixing process. In this case, the control unit 50 operates the crushing unit 20 while supplying water from the discharge unit 14, and causes the crushed material C stuck in the chute 21 to drop into the mixer 70. Thereafter, when the control unit 50 confirms that the abnormal state of the mixer 70 has been resolved, the normal operation of the mixer 70 is restarted. On the other hand, if the abnormal state of the mixer 70 has not been eliminated, the control unit 50 causes the notification unit 53 to notify that an abnormality has occurred in the mixing process, and stops the entire waste disposal apparatus 6.
 混合工程において、「ポリマー処理中」の状況が所定時間経過しても変化がない場合には、判定部51はポリマーと処理剤との反応が十分でないと判定する。この場合、制御部50は処理剤投入部23から追加の処理剤を投入させる制御を実行する。処理剤の投入量は反応が十分でないと判定した時点における第2測定部70Bの測定値に基づいて決定される。すなわち、判定部51は第2測定部70Bが測定したモータ70Aの消費電流の値に基づいて、紙おむつDdの状態としてのポリマーと処理剤とを反応させる処理の進行度を判定する。制御部50はこれに基づいて処理剤投入部23から再投入させる処理剤の投入量を決定する。 In the mixing step, if the state of “polymer processing” does not change even after the lapse of a predetermined time, the determination unit 51 determines that the reaction between the polymer and the processing agent is not sufficient. In this case, the control unit 50 executes control to cause the processing agent input unit 23 to input an additional processing agent. The input amount of the treatment agent is determined based on the measurement value of the second measurement unit 70B at the time when the reaction is determined to be insufficient. That is, the determination unit 51 determines the degree of progress of the process of causing the polymer in the state of the paper diaper Dd to react with the processing agent based on the value of the current consumption of the motor 70A measured by the second measurement unit 70B. The control unit 50 determines the amount of the processing agent to be re-input from the processing agent input unit 23 based on this.
 混合工程において、処理剤を再投入したにも関わらず「ポリマー処理中」の状況が所定時間経過しても変化しない場合には、判定部51は汚れの蓄積が発生したと判定(「要洗浄」と判定)する。この場合、制御部50は、ミキサ70の運転を停止し、ミキサ70の洗浄モードを実行する。ミキサ70の洗浄モードでは、制御部50は排出路11の第1開閉弁12を閉じた状態で、吐出部14から水を供給させるとともに処理剤投入部23から処理剤を投入させつつモータ70Aの正転及び逆転駆動を繰り返す制御を実行する。この洗浄モードにおいて投入される処理剤は第1処理剤投入部23Aから投入される酢酸カルシウムを含む処理剤のみである。その後、制御部50は、ミキサ70が「ポリマー処理済み」の状態になるまで、すなわち、第2測定部70Bが測定したモータ70Aの消費電流の大きさが所定値よりも小さくなるまでモータ70Aを正転駆動させる。制御部50は、ミキサ70の洗浄モードの実行中は、ミキサ70の洗浄モードを実行中であることを報知部53に報知させる。制御部50はミキサ70の状況が「ポリマー処理中」の状態から「ポリマー処理済み」の状態になったことを確認したら、報知部53による報知を停止する。一方、ミキサ70の異常状態が解消されない場合には、制御部50は、その旨を報知部53に報知させて汚物処理装置6全体を停止させる。 In the mixing step, when the state of “polymer processing” does not change even after the predetermined time has passed even though the processing agent is re-input, the determination unit 51 determines that accumulation of dirt has occurred (“cleaning required”). Is determined). In this case, the control unit 50 stops the operation of the mixer 70 and executes the cleaning mode of the mixer 70. In the cleaning mode of the mixer 70, the control unit 50 controls the motor 70A while supplying water from the discharge unit 14 and supplying the processing agent from the processing agent input unit 23 with the first on-off valve 12 of the discharge path 11 closed. The control for repeating the forward rotation and the reverse rotation drive is executed. The processing agent supplied in the cleaning mode is only the processing agent containing calcium acetate supplied from the first processing agent supply section 23A. Thereafter, the control unit 50 controls the motor 70A until the mixer 70 enters the “polymer-processed” state, that is, until the magnitude of the current consumption of the motor 70A measured by the second measurement unit 70B becomes smaller than a predetermined value. Drive forward. While the cleaning mode of the mixer 70 is being executed, the control unit 50 notifies the notification unit 53 that the cleaning mode of the mixer 70 is being executed. When the control unit 50 confirms that the state of the mixer 70 has changed from the “polymer processing” state to the “polymer processed” state, the control unit 50 stops the notification by the notification unit 53. On the other hand, if the abnormal state of the mixer 70 is not resolved, the control unit 50 notifies the notification unit 53 of the fact and stops the entire waste disposal apparatus 6.
 希釈工程において異常が発生した場合、例えば、希釈槽30の運転が開始されたにも関わらず「無負荷」の状況が所定時間経過しても変化がない場合には、判定部51は希釈工程において異常が発生したと判定する。具体的には、希釈槽30の上流側である排出路11において混合物Mの詰まりが発生した可能性が考えられる。この場合、制御部50は、希釈槽30の下流側である排水路15の第2開閉弁16を閉鎖した状態で、希釈槽30の上流側の第1開閉弁12の開閉を所定回数繰り返す制御を実行する。その後、制御部50は、希釈槽30の異常状態が解消されたことを確認したら、希釈槽30の通常の運転を再開する。一方、希釈槽30の異常状態が解消されなかった場合には、制御部50は、希釈工程において異常が発生したことを報知部53によって報知させ、汚物処理装置6全体を停止させる。 If an abnormality occurs in the dilution step, for example, if the state of “no load” does not change even after the predetermined time has passed even though the operation of the dilution tank 30 has been started, the determination unit 51 performs the dilution step. It is determined that an abnormality has occurred in. Specifically, it is conceivable that the mixture M may have clogged in the discharge path 11 on the upstream side of the dilution tank 30. In this case, the control unit 50 repeats the opening and closing of the first on-off valve 12 on the upstream side of the dilution tank 30 a predetermined number of times in a state where the second on-off valve 16 of the drainage channel 15 on the downstream side of the dilution tank 30 is closed. Execute After that, when the control unit 50 confirms that the abnormal state of the dilution tank 30 has been resolved, the normal operation of the dilution tank 30 is restarted. On the other hand, if the abnormal state of the dilution tank 30 has not been eliminated, the control unit 50 causes the notification unit 53 to notify that the abnormality has occurred in the dilution process, and stops the entire waste disposal apparatus 6.
 希釈工程において、制御部50は、「希釈処理中」の状況が所定時間経過しても変化がない場合には、希釈が十分でないと判定し、吐出部14から水を追加で供給させる制御を実行する。追加で供給する水の供給量は、希釈が十分でないと判定した時点における第3測定部30Dの測定値に基づいて決定される。すなわち、判定部51は第3測定部30Dが測定したモータ30Aの消費電流の値に基づいて、希釈槽30の状況(希釈処理の進行度)を判定する。制御部50はこれに基づいて吐出部14から再供給させる水の供給量を決定する。 In the dilution step, when the state of “dilution process” does not change even after the lapse of a predetermined time, the control unit 50 determines that the dilution is not sufficient, and performs control to additionally supply water from the discharge unit 14. Execute. The supply amount of the water to be additionally supplied is determined based on the measurement value of the third measurement unit 30D at the time when the dilution is determined to be insufficient. That is, the determination unit 51 determines the state of the dilution tank 30 (the degree of progress of the dilution process) based on the value of the current consumption of the motor 30A measured by the third measurement unit 30D. The control unit 50 determines the supply amount of water to be resupplied from the discharge unit 14 based on this.
 希釈工程において、水を再供給したにも関わらず「希釈処理中」の状況が所定時間経過しても変化しない場合には、判定部51は希釈槽30において汚れの蓄積が発生したと判定(「要洗浄」と判定)する。この場合、制御部50は、希釈槽30の運転を停止し、希釈槽30の洗浄モードを実行する。希釈槽30の洗浄モードでは、制御部50は、排出路11の第1開閉弁12を開いた状態、且つ排水路15の第2開閉弁16を閉じた状態で、吐出部14から水を供給させるとともに処理剤投入部23から処理剤を投入させつつ、ミキサ70のモータ70A及び希釈槽30のモータ30Aの正転及び逆転駆動をそれぞれ繰り返す制御を実行する。この洗浄モードにおいて投入される処理剤は第1処理剤投入部23Aから投入される酢酸カルシウムを含む処理剤のみである。その後、制御部50は、希釈槽30が「希釈処理済み」の状態になるまで、すなわち、第3測定部30Dが測定したモータ30Aの消費電流の大きさが第2の所定値以上でない状態になるまでモータ70A及びモータ30Aを駆動させる。希釈槽30の洗浄モードの実行中は、制御部50は希釈槽30の洗浄モードを実行中であることを報知部53に報知させる。制御部50は、希釈槽30の状況が「希釈処理済み」の状態になったことを確認したら、報知部53による報知を停止する。一方、希釈槽30の異常状態が解消されない場合には、制御部50はその旨を報知部53に報知させて汚物処理装置6全体を停止する。 In the dilution step, when the state of “dilution process” does not change even after the predetermined time has passed even though water is resupplied, the determination unit 51 determines that accumulation of dirt has occurred in the dilution tank 30 ( It is determined that “cleaning is required”). In this case, the control unit 50 stops the operation of the dilution tank 30 and executes the cleaning mode of the dilution tank 30. In the washing mode of the dilution tank 30, the control unit 50 supplies water from the discharge unit 14 in a state where the first opening / closing valve 12 of the discharge passage 11 is open and a state where the second opening / closing valve 16 of the drain passage 15 is closed. At the same time, while the processing agent is being injected from the processing agent input section 23, the control for repeating the forward rotation and the reverse rotation driving of the motor 70A of the mixer 70 and the motor 30A of the dilution tank 30, respectively, is executed. The processing agent supplied in the cleaning mode is only the processing agent containing calcium acetate supplied from the first processing agent supply section 23A. Thereafter, the control unit 50 keeps the state until the dilution tank 30 is in the “diluted” state, that is, the state in which the magnitude of the current consumption of the motor 30A measured by the third measuring unit 30D is not equal to or more than the second predetermined value. The motor 70A and the motor 30A are driven until the operation is completed. While the cleaning mode of the dilution tank 30 is being executed, the control unit 50 notifies the notification unit 53 that the cleaning mode of the dilution tank 30 is being executed. When the control unit 50 confirms that the state of the dilution tank 30 is in the state of “diluted”, the control unit 50 stops the notification by the notification unit 53. On the other hand, if the abnormal state of the dilution tank 30 is not resolved, the control unit 50 notifies the notification unit 53 of the fact and stops the entire waste disposal apparatus 6.
 分離工程において異常が発生した場合、例えば、分離部40の運転が開始されたにも関わらず「無負荷」の状況から所定時間経過しても変化がない場合には、判定部51は異常が発生したと判定する。具体的には、分離部40の上流側である排水路15において希釈物Tの詰まりが発生した可能性が考えられる。この場合、制御部50は分離部40を運転しつつ第2開閉弁16の開閉を所定回数繰り返す制御を実行する。その間、制御部50は分離工程にて異常が発生したことを報知部53によって報知させる。その後、制御部50は、分離部40の異常状態が解消されたことを確認したら、分離部40の通常の運転を再開する。一方、分離部40の異常状態が解消されなかった場合には、制御部50は、分離工程にて異常が発生したことを報知部53によって報知させ、汚物処理装置6全体を停止させる。 When an abnormality occurs in the separation process, for example, when the operation of the separation unit 40 is started and there is no change after a lapse of a predetermined time from the “no load” state, the determination unit 51 determines that the abnormality is It is determined that an error has occurred. Specifically, it is conceivable that the diluent T may have clogged in the drainage channel 15 on the upstream side of the separation unit 40. In this case, the control unit 50 executes control to repeat opening and closing of the second on-off valve 16 a predetermined number of times while operating the separation unit 40. Meanwhile, the control unit 50 causes the notification unit 53 to notify that an abnormality has occurred in the separation process. Thereafter, when the control unit 50 confirms that the abnormal state of the separation unit 40 has been resolved, the normal operation of the separation unit 40 is restarted. On the other hand, when the abnormal state of the separation unit 40 has not been eliminated, the control unit 50 causes the notification unit 53 to notify that the abnormality has occurred in the separation process, and stops the entire waste disposal apparatus 6.
 分離工程において、分離部40の状況が「分離処理中」である状態から、所定時間内に、「無負荷」である状態にならなかった場合、判定部51は分離部40において汚れの蓄積が発生したと判定(「要洗浄」と判定)する。この場合、制御部50は分離部40の洗浄モードを実行する。分離部40の洗浄モードでは、制御部50は、排出路11の第1開閉弁12及び排水路15の第2開閉弁16を開いた状態で、吐出部14から水を供給させるとともに処理剤投入部23から処理剤を投入させつつ、ミキサ70のモータ70A、希釈槽30のモータ30A、及び分離部40のモータ40Cの正転及び逆転駆動をそれぞれ繰り返す制御を実行する。この洗浄モードにおいて投入される処理剤は第1処理剤投入部23Aから投入される酢酸カルシウムを含む処理剤のみである。その後、制御部50は分離部40が「無負荷」の状態になるまで、すなわち、第4測定部40Fが測定したモータ40Cの消費電流の大きさが所定値以上でない状態になるまでモータ70A、モータ30A、及びモータ40Cをそれぞれ駆動させる。分離部40の洗浄モードの実行中は、制御部50は分離部40の洗浄モードを実行中であることを報知部53に報知させる。制御部50は、分離部40の状況が「無負荷」の状態になったことを確認したら、報知部53による報知を停止する。一方、分離部40の異常状態が解消されない場合には、制御部50はその旨を報知部53に報知させて汚物処理装置6全体を停止する。 In the separation step, if the state of the separation unit 40 does not change from the state of “separation processing” to the state of “no load” within a predetermined time, the determination unit 51 determines that accumulation of dirt in the separation unit 40 has not occurred. It is determined that the occurrence has occurred (determined as "needs cleaning"). In this case, the control unit 50 executes the cleaning mode of the separation unit 40. In the cleaning mode of the separation unit 40, the control unit 50 controls the supply of water from the discharge unit 14 and the input of the treatment agent with the first on-off valve 12 of the discharge path 11 and the second on-off valve 16 of the drainage path 15 opened. While the processing agent is supplied from the unit 23, control is performed to repeat the forward rotation and the reverse rotation of the motor 70 A of the mixer 70, the motor 30 A of the dilution tank 30, and the motor 40 C of the separation unit 40, respectively. The processing agent supplied in the cleaning mode is only the processing agent containing calcium acetate supplied from the first processing agent supply section 23A. Thereafter, the control unit 50 controls the motors 70A and 70A until the separation unit 40 is in the “no load” state, that is, until the magnitude of the current consumption of the motor 40C measured by the fourth measurement unit 40F is not a predetermined value or more. The motor 30A and the motor 40C are each driven. During the execution of the cleaning mode of the separation unit 40, the control unit 50 causes the notification unit 53 to notify that the cleaning mode of the separation unit 40 is being executed. When the control unit 50 confirms that the state of the separation unit 40 has become “no load”, the control unit 50 stops the notification by the notification unit 53. On the other hand, when the abnormal state of the separation unit 40 is not eliminated, the control unit 50 notifies the notification unit 53 of the fact and stops the entire waste disposal apparatus 6.
 上述のように、汚物処理装置6は、処理部90による各処理の実行時、破砕部20、ミキサ70、希釈槽30、及び分離部40のいずれかにおいて処理の開始から一定時間経過後の第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fによる測定値が想定値と異なる場合、制御部50は測定値と想定値との差に基づいて、処理剤の追加投入及び水の追加供給の少なくとも一方を実行させる。 As described above, at the time of execution of each processing by the processing unit 90, the waste disposal apparatus 6 performs the second processing after a predetermined time has elapsed from the start of the processing in any of the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40. When the measurement values of the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 40F are different from the assumed values, the control unit 50 performs processing based on the difference between the measurement values and the assumed values. At least one of the additional introduction of the agent and the additional supply of water is executed.
 制御部50は汚物処理装置6によって紙おむつDdの処理が行われている間、その稼働状況を報知部53に報知させる制御を実行する。本実施形態の場合、制御部50は、汚物処理装置6の稼働状況として、上述のような異常発生時の異常内容の他に、処理部90による処理が正常である場合には、処理が正常に行われていること、現在の工程、終了までの時間、であることを報知部53に報知させる。制御部50は、これら汚物処理装置6の各種稼働状況に関する情報をデータとして記憶部54に記憶させるとともに、送信部55に外部送信させる。 The control unit 50 executes a control to notify the operating unit 53 of the operation status while the waste disposal apparatus 6 is processing the paper diaper Dd. In the case of the present embodiment, the control unit 50 determines that the operation status of the processing unit 90 is normal if the processing by the processing unit 90 is normal in addition to the abnormality content at the time of occurrence of the abnormality as described above as the operation status of the waste disposal apparatus 6. , The current process, and the time to the end are notified to the notifying unit 53. The control unit 50 causes the storage unit 54 to store information regarding various operating states of the waste disposal apparatus 6 as data, and causes the transmission unit 55 to transmit the information externally.
 次に、制御部50による処理部90の状況の予測について説明する。上述のように、処理部90の各部は処理開始から終了までの間の処理の進行の程度に応じたモータの負荷変動が生じる。図9は、処理部90の各部としてのミキサ70において、被処理物としての紙おむつDdを処理する際の処理回数(横軸)とモータ70Aの負荷低減時間(縦軸)との関係を示している。負荷低減時間とは、処理部90の各部において、処理を開始して一旦上昇したモータの消費電流値が所定値まで低下するまでの時間である。ミキサ70の場合、モータ70Aの消費電流値はポリマーと処理剤との反応が進行するにつれて低下する。モータ70Aの消費電流値はミキサ70において正常な処理が行われている時には、所定時間内に所定値以下に減少する。しかし、汚れが蓄積したり、何らかの異常が生じたりすると、所定時間内にモータ70Aの負荷が所定値まで減少しなくなる。この場合、以降の正常な処理を行うことができなくなるおそれがある。このため、本実施形態では、運転状態に関する情報としての負荷低減時間を測定部によって測定される運転状態に関する情報に基づいて制御部50が取得し、この負荷低減時間を測定して記憶部54に記憶させるとともに、記憶部54に記憶させた過去の負荷低減時間に基づいて、制御部50によってミキサ70の未来の状況を予測する。すなわち、制御部50は処理部の運転状態に関する情報を取得する情報取得部として、第2測定部70Bが測定したモータ70Aの消費電流の大きさに基づいて負荷低減時間を取得する。判定部51は処理部の運転状態に関する情報としての負荷低減時間に基づいて、ミキサ70における処理の状況を判定する。更に、判定部51は記憶部54に記憶された過去の負荷低減時間に基づいて、ミキサ70における処理の状況を予測する。 Next, prediction of the state of the processing unit 90 by the control unit 50 will be described. As described above, in each unit of the processing unit 90, the motor load varies according to the degree of progress of the process from the start to the end of the process. FIG. 9 shows the relationship between the number of times of processing (horizontal axis) and the load reduction time (vertical axis) of the motor 70A when processing the disposable diaper Dd as an object to be processed in the mixer 70 as each unit of the processing unit 90. I have. The load reduction time is a time from when the processing is started in each unit of the processing unit 90 until the current consumption value of the motor, which has risen once, decreases to a predetermined value. In the case of the mixer 70, the current consumption value of the motor 70A decreases as the reaction between the polymer and the processing agent progresses. The current consumption value of the motor 70A decreases to a predetermined value or less within a predetermined time when a normal process is performed in the mixer 70. However, if dirt accumulates or some abnormality occurs, the load on the motor 70A does not decrease to a predetermined value within a predetermined time. In this case, the subsequent normal processing may not be performed. For this reason, in the present embodiment, the control unit 50 acquires the load reduction time as the information on the operation state based on the information on the operation state measured by the measurement unit, measures the load reduction time, and stores it in the storage unit 54. The control unit 50 predicts the future state of the mixer 70 based on the past load reduction time stored in the storage unit 54 while storing the same. That is, the control unit 50 obtains the load reduction time based on the magnitude of the current consumption of the motor 70A measured by the second measuring unit 70B as an information obtaining unit that obtains information on the operation state of the processing unit. The determination unit 51 determines the state of the processing in the mixer 70 based on the load reduction time as information on the operation state of the processing unit. Further, the determination unit 51 predicts the processing status of the mixer 70 based on the past load reduction time stored in the storage unit 54.
 具体的には、制御部50は、ミキサ70によって処理が完了した時点で、第2測定部70Bが測定したモータ70Aの消費電流値に基づいて負荷低減時間を取得するとともに、記憶部54に記憶させた過去の負荷低減時間のうちの直近の複数回(例えば、10回)分の測定値とを直線回帰によって回帰分析して、あと何回(例えば、20回)以内で上限値を超過するか否かを予測する。図9の場合、最も新しい測定値Mvを含む直近の10回分の負荷低減時間を直線回帰によって回帰分析すると、20回以内(18回)で上限値を超過することが予測される例である。このような予測結果となった場合には、判定部51はミキサ70の洗浄が必要な状況であると判定する。この場合、制御部50はミキサ70の洗浄モードを実行する。このとき、制御部50は報知部53による報知を実行させる。 Specifically, when the processing is completed by the mixer 70, the control unit 50 acquires the load reduction time based on the current consumption value of the motor 70A measured by the second measurement unit 70B, and stores the load reduction time in the storage unit 54. A regression analysis is performed by linear regression on the measured values of a plurality of recent times (for example, 10 times) of the past load reduction times, and the upper limit value is exceeded within several times (for example, 20 times). Predict whether or not. In the case of FIG. 9, when the regression analysis is performed by linear regression on the last ten load reduction times including the newest measured value Mv, it is predicted that the upper limit will be exceeded within 20 times (18 times). When such a prediction result is obtained, the determination unit 51 determines that the situation requires the cleaning of the mixer 70. In this case, the control unit 50 executes the cleaning mode of the mixer 70. At this time, the control unit 50 causes the notification unit 53 to execute notification.
 判定部51による処理部90の状況の予測はミキサ70のみならず、破砕部20、希釈槽30、及び分離部40でも同様に行うことができる。破砕部20の場合、第1測定部20Hが測定したモータ20Gの消費電流値に基づいて取得した負荷低減時間が所定範囲内にあるか否かを判定することができるとともに、過去に取得した負荷低減時間のうちの直近の複数回分の数値を回帰分析することによって所定回数以内で上限値を超過するか否かを予測することができる。希釈槽30の場合、第3測定部30Dが測定したモータ30Aの消費電流値に基づいて取得した負荷低減時間が所定範囲内にあるか否かを判定することができるとともに、過去に取得した負荷低減時間のうちの直近の複数回分の数値を回帰分析することによって所定回数以内で上限値を超過するか否かを予測することができる。分離部40の場合、第4測定部40Fが測定したモータ40Cの消費電流値に基づいて取得した負荷低減時間が所定範囲内にあるか否かを判定することができるとともに、過去に取得した負荷低減時間のうちの直近の複数回分の数値を回帰分析することによって所定回数以内で上限値を超過するか否かを予測することができる。 The prediction of the state of the processing unit 90 by the determination unit 51 can be similarly performed not only in the mixer 70 but also in the crushing unit 20, the dilution tank 30, and the separation unit 40. In the case of the crushing unit 20, it is possible to determine whether the load reduction time acquired based on the current consumption value of the motor 20G measured by the first measuring unit 20H is within a predetermined range, and to determine the load acquired in the past. By performing a regression analysis on the numerical values for the latest plurality of times in the reduction time, it is possible to predict whether or not the upper limit value is exceeded within a predetermined number of times. In the case of the dilution tank 30, it is possible to determine whether or not the load reduction time acquired based on the current consumption value of the motor 30A measured by the third measuring unit 30D is within a predetermined range, and to determine the load acquired in the past. By performing a regression analysis on the numerical values for the latest plurality of times in the reduction time, it is possible to predict whether or not the upper limit value is exceeded within a predetermined number of times. In the case of the separation unit 40, it is possible to determine whether the load reduction time acquired based on the current consumption value of the motor 40C measured by the fourth measurement unit 40F is within a predetermined range, and to determine the load acquired in the past. By performing a regression analysis on the numerical values for the latest plurality of times in the reduction time, it is possible to predict whether or not the upper limit value is exceeded within a predetermined number of times.
 判定部51による処理部90の状況の予測は、例えば、図10に例示するように、運転状態に関する情報として、第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fによって測定した消費電流値と、直近の複数回(例えば、10回)分の消費電力値の測定値とを直線回帰によって回帰分析することによって、あと何回(例えば、20回)以内に上限値及び下限値の少なくともいずれか一方を超過するか否か予測することもできる。 For example, as illustrated in FIG. 10, the prediction of the state of the processing unit 90 by the determination unit 51 includes, as information on the operating state, the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit 30D. By performing regression analysis by linear regression on the current consumption value measured by the measurement unit 40F and the measured values of the power consumption values of the latest multiple times (for example, 10 times), within several times (for example, 20 times) It is also possible to predict whether or not at least one of the upper limit value and the lower limit value will be exceeded.
 以上のように、第4の汚物処理装置の実施形態6の汚物処理装置6は、投入部10から投入された被処理物としての紙おむつDdの状態を判定し、その判定した状態に基づいて処理剤の投入量を決定する。このため、処理剤の適正な量を容易に把握することができる。 As described above, the waste disposal apparatus 6 according to the sixth embodiment of the fourth waste disposal apparatus determines the state of the disposable diaper Dd as the processing object input from the input unit 10, and performs processing based on the determined state. Determine the dosage of the agent. Therefore, an appropriate amount of the treatment agent can be easily grasped.
 したがって、第4の汚物処理装置の実施形態6の汚物処理装置6は、処理剤の過不足による不具合の発生を抑制することができる。 Therefore, the waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus can suppress the occurrence of trouble due to excess or deficiency of the treatment agent.
 以上のように、第5の汚物処理装置の実施形態6の汚物処理装置6は、情報取得部としての制御部50によって、第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fによって測定された処理部90の各部(破砕部20、ミキサ70、希釈槽30、及び分離部40)の各モータ20G,70A,30A,40Cの消費電流値が取得される。この消費電流値は記憶部54に記憶される。判定部51は、制御部50が取得した処理部90の運転状態に関する情報としての消費電流値に基づいて処理部90の状況を判定する。このように、判定部51によって処理部90の状況が判定されるので、作業者が判定する場合と比較して、判定結果のばらつきを低減することができる。 As described above, the waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus has the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the control unit 50 as the information acquisition unit. And the current consumption values of the motors 20G, 70A, 30A, and 40C of the respective units (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) measured by the fourth measuring unit 40F. . This consumed current value is stored in the storage unit 54. The determination unit 51 determines the state of the processing unit 90 based on the current consumption value as information on the operating state of the processing unit 90 acquired by the control unit 50. As described above, since the state of the processing unit 90 is determined by the determination unit 51, it is possible to reduce the variation in the determination result as compared with the case where the operator determines.
 したがって、第5の汚物処理装置の実施形態6の汚物処理装置6は、処理部90の状況をより正確に把握することができる。 Therefore, the waste disposal apparatus 6 of the sixth embodiment of the fifth waste disposal apparatus can more accurately grasp the status of the processing unit 90.
 第4の汚物処理装置の実施形態6の汚物処理装置6は、処理部90に処理剤を投入する処理剤投入部23と、投入部10から投入された紙おむつDdの個数を計測する計測部52とを備えている。判定部51は、計測部52の計測結果に基づいて紙おむつDdの状態を判定する。制御部50は、決定した投入量の処理剤を処理剤投入部23から投入させる。このため、計測部52によって、投入した直後に紙おむつDdの個数を計測することができるので、状態の判定を速やかに行うことができる。制御部50は、この判定結果に基づいた適正な量の処理剤を処理剤投入部23から投入させる。これによって、処理剤を速やか且つ適正に投入して処理を行うことができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fourth waste disposal apparatus includes a treatment agent input section 23 that inputs a processing agent into the processing section 90 and a measurement section 52 that measures the number of disposable diapers Dd input from the input section 10. And The determination unit 51 determines the state of the paper diaper Dd based on the measurement result of the measurement unit 52. The control unit 50 causes the processing agent input unit 23 to input the determined input amount of the processing agent. For this reason, the number of disposable diapers Dd can be measured by the measuring unit 52 immediately after the dispensing, so that the state can be quickly determined. The control unit 50 causes the processing agent input unit 23 to input an appropriate amount of the processing agent based on the determination result. As a result, the processing agent can be promptly and appropriately charged to perform the processing.
 第4の汚物処理装置の実施形態6の汚物処理装置6において、制御部50は、決定した投入量に対して、処理剤投入部23が投入可能な処理剤の量の不足を検出したときには、処理部90の運転を停止する。このため、水分を吸収可能な状態の処理剤と未反応のポリマーが排出されてしまうのを防止することができる。 In the waste disposal apparatus 6 of the sixth embodiment of the fourth waste disposal apparatus, when the control unit 50 detects the shortage of the amount of the processing agent that can be injected with respect to the determined injection amount, The operation of the processing unit 90 is stopped. For this reason, it is possible to prevent the treatment agent in a state capable of absorbing moisture and the polymer that has not reacted to be discharged.
 第4の汚物処理装置の実施形態6の汚物処理装置6は、汚物処理装置6の稼働状況に関する情報を報知する報知部53を備えている。このため、使用者による汚物処理装置6の稼働状況の容易な把握を支援することができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fourth waste disposal apparatus is provided with a notification unit 53 that reports information on the operation status of the waste disposal apparatus 6. Therefore, it is possible to assist the user in easily grasping the operation status of the waste disposal apparatus 6.
 第4の汚物処理装置の実施形態6の汚物処理装置6は、汚物処理装置6の稼働状況に関する情報を記憶する記憶部54を備えている。このため、使用者に過去の稼働状況を容易に知らしめることができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fourth waste disposal apparatus includes a storage unit 54 for storing information on the operation status of the waste disposal apparatus 6. For this reason, the user can be easily notified of the past operation status.
 第4の汚物処理装置の実施形態6の汚物処理装置6は、汚物処理装置6の稼働状況を外部に送信する送信部55を備えている。このため、汚物処理装置6の稼働状況を外部から把握することができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fourth waste disposal apparatus includes a transmission unit 55 that transmits the operating status of the waste disposal apparatus 6 to the outside. Therefore, the operation status of the waste disposal apparatus 6 can be grasped from outside.
 第4の汚物処理装置の実施形態6の汚物処理装置6において、制御部50は、破砕部20における処理時間を計測し、この計測結果に応じた処理剤の追加投入量を決定するとともに、決定した投入量の処理剤を処理剤投入部23から投入させる。このため、適正な処理を確実に行うことができる。 In the waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus, the control unit 50 measures the processing time in the crushing unit 20, determines the additional amount of the processing agent according to the measurement result, and determines the amount. The processing agent of the supplied amount is injected from the processing agent input unit 23. Therefore, appropriate processing can be reliably performed.
 第4の汚物処理装置の実施形態6の汚物処理装置6は、情報取得部としての制御部50によって、第1測定部20H、第2測定部70B、第3測定部30D、及び第4測定部40Fによって測定された処理部90の各部(破砕部20、ミキサ70、希釈槽30、及び分離部40)の各モータ20G,70A,30A,40Cの消費電流値が取得される。この消費電流値は記憶部54に記憶される。判定部51は、制御部50が取得した処理部90の運転状態に関する情報としての消費電流値に基づいて処理部90の状況を判定する。このように、判定部51によって処理部90の状況が判定されるので、作業者が判定する場合と比較して、判定結果のばらつきを低減することができる。その結果、処理部90の状況をより正確に把握することができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fourth waste disposal apparatus is configured such that the control unit 50 as the information acquisition unit controls the first measurement unit 20H, the second measurement unit 70B, the third measurement unit 30D, and the fourth measurement unit. The current consumption values of the motors 20G, 70A, 30A, and 40C of the respective units of the processing unit 90 (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) measured by 40F are acquired. This consumed current value is stored in the storage unit 54. The determination unit 51 determines the state of the processing unit 90 based on the current consumption value as information on the operating state of the processing unit 90 acquired by the control unit 50. As described above, since the state of the processing unit 90 is determined by the determination unit 51, it is possible to reduce the variation in the determination result as compared with the case where the operator determines. As a result, the status of the processing unit 90 can be grasped more accurately.
 第4の汚物処理装置の実施形態6の汚物処理装置6において、判定部51は、記憶部54に記憶された過去の運転状態に関する情報に基づいて、処理部90の状況を予測する。このため、処理部90が異常状態で運転されることの未然防止を図ることができる。 In the waste disposal apparatus 6 of the sixth embodiment of the fourth waste disposal apparatus, the determination unit 51 predicts the state of the processing unit 90 based on the information on the past operation state stored in the storage unit 54. Therefore, it is possible to prevent the processing unit 90 from operating in an abnormal state.
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6は、判定部51によって予測された処理部90の状況が所定の状況である場合、すなわち、処理部90の各部(破砕部20、ミキサ70、希釈槽30、及び分離部40)の負荷低減時間が所定値を超えることが予測された場合には、処理部90の各部を洗浄する洗浄運転としての洗浄モードを実行する。このため、処理部90における異常の発生を抑制することができる。 The waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, when the situation of the processing unit 90 predicted by the determination unit 51 is a predetermined situation, that is, When it is predicted that the load reduction time of each unit (the crushing unit 20, the mixer 70, the dilution tank 30, and the separation unit 40) exceeds a predetermined value, a cleaning mode as a cleaning operation for cleaning each unit of the processing unit 90. Execute For this reason, occurrence of an abnormality in the processing unit 90 can be suppressed.
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6は、判定部51によって予測された処理部90の状況が所定の状況である場合、すなわち、処理部90の各部(破砕部20、ミキサ70、希釈槽30、及び分離部40)のモータ20G,70A,30A,40Cの消費電流値が所定値を超えることが予測された場合には、処理部90の各部を洗浄する洗浄運転としての洗浄モードを実行する。このため、処理部90における異常の発生を抑制することができる。 The waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, when the situation of the processing unit 90 predicted by the determination unit 51 is a predetermined situation, that is, If it is predicted that the current consumption of the motors 20G, 70A, 30A, and 40C of each part (the crushing part 20, the mixer 70, the dilution tank 30, and the separation part 40) exceeds a predetermined value, each part of the processing part 90 A cleaning mode as a cleaning operation for cleaning is performed. For this reason, occurrence of an abnormality in the processing unit 90 can be suppressed.
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6において、判定部51は、洗浄モードを行った後に処理部90の状況を再判定する。このため、処理部90の異常状態が解消されたか否かを確実に把握することができる。 に お い て In the waste disposal apparatus 6 of Embodiment 6 of the fourth and fifth waste disposal apparatuses, the determination unit 51 re-determines the status of the processing unit 90 after performing the cleaning mode. For this reason, it is possible to reliably grasp whether or not the abnormal state of the processing unit 90 has been resolved.
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6は、運転状態に関する情報を外部に送信する送信部55を備えている。このため、処理部90の状況を外部から把握することができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fourth and fifth waste disposal apparatuses is provided with a transmission unit 55 that transmits information on the operating state to the outside. Therefore, the status of the processing unit 90 can be grasped from outside.
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6において、送信部55は、複数の汚物処理装置の送信部から送信された各処理部の運転状態に関する情報を受信する外部の受信部に、運転状態に関する情報を送信する。このため、複数の装置の処理部の状況を管理する管理センターの管理機器等に処理部90の運転状態に関する情報を送信することができる。 In the filth disposal apparatus 6 of Embodiment 6 of the fourth filth disposal apparatus and the fifth filth disposal apparatus, the transmission unit 55 transmits the information on the operation state of each processing unit transmitted from the transmission units of the plurality of filth disposal apparatuses. The information about the operating state is transmitted to an external receiving unit that receives the information. Therefore, it is possible to transmit information on the operation state of the processing unit 90 to a management device or the like of a management center that manages the states of the processing units of the plurality of devices.
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6において、処理部としてのミキサ70、希釈槽30、及び分離部40のそれぞれは、制御部50によって異常状態であることが自動的に判定されてそれらを解消するための運転モードである洗浄モードが自動的に開始される。このため、汚物処理装置6のメンテナンスに係る手間の低減を図ることができる。 In the waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, each of the mixer 70, the dilution tank 30, and the separation unit 40 as a processing unit is in an abnormal state by the control unit 50. It is automatically determined that there is, and a washing mode, which is an operation mode for eliminating them, is automatically started. For this reason, it is possible to reduce the labor involved in the maintenance of the waste disposal apparatus 6.
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6は、処理剤として酢酸カルシウムを用いている。このため、ホットメルト等の粘着剤の成分が被処理物である紙おむつDdに含まれている場合に、回転刃等による圧力や摺動を伴った粘着剤の成分が付着し易い処理において、酢酸の作用によって粘着剤の付着を抑制することができる。粘着剤が付着した場合でも剥がれ易くなり、好適に除去することができる。 汚 The waste disposal apparatus 6 of Embodiment 6 of the fourth and fifth waste disposal apparatuses uses calcium acetate as a treatment agent. For this reason, when the components of the adhesive such as hot melt are contained in the disposable diaper Dd to be processed, the acetic acid is used in a process in which the components of the adhesive accompanied by pressure or sliding by a rotary blade or the like are likely to adhere. Can suppress the adhesion of the pressure-sensitive adhesive. Even when the adhesive is adhered, the adhesive is easily peeled off and can be suitably removed.
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6は、ポリマーの吸水性能を抑制するための塩化カルシウムを含む処理剤を投入する第2処理剤投入部23Bを備えている。このため、塩化カルシウムよりも高価な酢酸カルシウムを含む処理剤のみを用いて処理する場合と比較して、コストダウンを図ることができる。 The waste disposal apparatus 6 of Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus is provided with a second treatment agent introduction part 23B for introducing a treatment agent containing calcium chloride for suppressing the water absorption performance of the polymer. Have. Therefore, the cost can be reduced as compared with the case where the treatment is performed using only the treatment agent containing calcium acetate which is more expensive than calcium chloride.
 第4の汚物処理装置及び第5の汚物処理装置の実施形態6の汚物処理装置6は、処理剤として酢酸カルシウムを用いている。このため、酢酸の殺菌作用によって、装置を衛生的な状態に保つことができる。 汚 The waste disposal apparatus 6 of Embodiment 6 of the fourth and fifth waste disposal apparatuses uses calcium acetate as a treatment agent. Therefore, the device can be kept in a sanitary state by the bactericidal action of acetic acid.
 第5の汚物処理装置の実施形態6の汚物処理装置6において、判定部51は、記憶部54に記憶された過去の運転状態に関する情報としての負荷低減時間に基づいて、処理部90の状況を予測する。このため、処理部90が異常状態で運転されることの未然防止を図ることができる。 In the waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus, the determination unit 51 determines the status of the processing unit 90 based on the load reduction time stored in the storage unit 54 as the information on the past operation state. Predict. Therefore, it is possible to prevent the processing unit 90 from operating in an abnormal state.
 第5の汚物処理装置の実施形態6の汚物処理装置6は、投入部10から投入された被処理物としての紙おむつDdの状態を判定し、その判定した状態に基づいて処理剤投入部23から投入する処理剤の投入量を決定する。このため、処理剤の適正な量を容易に把握することができる。その結果、処理剤の過不足による不具合の発生を抑制することができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus determines the state of the disposable diaper Dd as an object to be treated introduced from the introduction section 10 and, based on the determined state, from the treatment agent introduction section 23. The amount of the processing agent to be charged is determined. Therefore, an appropriate amount of the treatment agent can be easily grasped. As a result, it is possible to suppress the occurrence of a problem due to excess or deficiency of the processing agent.
 第5の汚物処理装置の実施形態6の汚物処理装置6は、処理部90に処理剤を投入する処理剤投入部23と、投入部10から投入された紙おむつDdの個数を計測する計測部52とを備えている。判定部51は、計測部52の計測結果に基づいて紙おむつDdの状態を判定する。制御部50は、決定した投入量の処理剤を処理剤投入部23から投入させる。このため、計測部52によって、投入した直後に紙おむつDdの個数を計測することができるので、状態の判定を速やかに行うことができる。制御部50は、この判定結果に基づいた適正な量の処理剤を処理剤投入部23から投入させる。これによって、処理剤を速やか且つ適正に投入して処理を行うことができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus includes a processing agent input section 23 for inputting a processing agent to the processing section 90 and a measuring section 52 for measuring the number of disposable diapers Dd input from the input section 10. And The determination unit 51 determines the state of the paper diaper Dd based on the measurement result of the measurement unit 52. The control unit 50 causes the processing agent input unit 23 to input the determined input amount of the processing agent. For this reason, the number of disposable diapers Dd can be measured by the measuring unit 52 immediately after the dispensing, so that the state can be quickly determined. The control unit 50 causes the processing agent input unit 23 to input an appropriate amount of the processing agent based on the determination result. As a result, the processing agent can be promptly and appropriately charged to perform the processing.
 第5の汚物処理装置の実施形態6の汚物処理装置6において、制御部50は、決定した投入量に対して、処理剤投入部23が投入可能な処理剤の量の不足を検出したときには、処理部90の運転を停止する。このため、水分を吸収可能な状態の処理剤と未反応のポリマーが排出されてしまうのを防止することができる。 In the waste disposal apparatus 6 of the sixth embodiment of the fifth waste disposal apparatus, when the control unit 50 detects the shortage of the amount of the processing agent that can be injected with respect to the determined injection amount, The operation of the processing unit 90 is stopped. For this reason, it is possible to prevent the treatment agent in a state capable of absorbing moisture and the polymer that has not reacted to be discharged.
 第5の汚物処理装置の実施形態6の汚物処理装置6は、汚物処理装置6の稼働状況に関する情報を報知する報知部53を備えている。このため、使用者による汚物処理装置6の稼働状況の容易な把握を支援することができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus is provided with a notification unit 53 that reports information on the operation status of the waste disposal apparatus 6. Therefore, it is possible to assist the user in easily grasping the operation status of the waste disposal apparatus 6.
 第5の汚物処理装置の実施形態6の汚物処理装置6は、記憶部54は、汚物処理装置6の稼働状況に関する情報を記憶する。このため、使用者に過去の稼働状況を容易に知らしめることができる。 汚 In the waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus, the storage unit 54 stores information on the operation status of the waste disposal apparatus 6. For this reason, the user can be easily notified of the past operation status.
 第5の汚物処理装置の実施形態6の汚物処理装置6は、汚物処理装置6の稼働状況を外部に送信する送信部55を備えている。このため、汚物処理装置6の稼働状況を外部から把握することができる。 The waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus includes a transmission unit 55 that transmits the operating status of the waste disposal apparatus 6 to the outside. Therefore, the operation status of the waste disposal apparatus 6 can be grasped from outside.
 第5の汚物処理装置の実施形態6の汚物処理装置6において、制御部50は、破砕部20における処理時間を計測し、この計測結果に応じた処理剤の追加投入量を決定するとともに、決定した投入量の処理剤を処理剤投入部23から投入させる。このため、適正な処理を確実に行うことができる。 In the waste disposal apparatus 6 according to the sixth embodiment of the fifth waste disposal apparatus, the control unit 50 measures the processing time in the crushing unit 20, determines the additional input amount of the processing agent according to the measurement result, and determines the amount. The processing agent of the supplied amount is injected from the processing agent input unit 23. Therefore, appropriate processing can be reliably performed.
 第1の汚物処理装置は上記記述及び図面によって説明した実施形態1から3に限定されるものではなく、例えば次のような実施形態も第1の汚物処理装置の技術的範囲に含まれる。
(1)第1の汚物処理装置の実施形態1では、脱臭装置が送風部を有している。しかし、これに限らず、吸気部の他端面から、脱臭部を介在させて、第2接続口に連通する送風路を設けてもよい。さらに、この送風路に、第2接続口から吸気部に向けて空気が流れることを制限し、吸気部から第2接続口に向けて空気が流れることを制限しない制限部を設け、制限部と脱臭部との間に排気口を設けてもよい。
(2)第1の汚物処理装置の実施形態1では、脱臭装置が送風部を有している。しかし、これに限らず、実施形態1の構成から送風部を除いた構成としてもよい。
(3)第1の汚物処理装置の実施形態1では、脱臭装置が送風部を有している。しかし、これに限らず、投入部に第3接続口を形成し、この第3接続口と送風部の一端面とを送風路で接続して連通させてもよい。
(4)第1の汚物処理装置の実施形態1では、第2通気路の一端が第1通気路に連通している。しかし、これに限らず、第2通気路の一端が投入部に接続され、他端が分離部に接続されていてもよい。
(5)第1の汚物処理装置の実施形態1では、第3通気路に吸気部を設けている。しかし、これに限らず、吸気部に代えて、脱臭部を設けてもよく、吸気部と脱臭部とを併用してもよい。
(6)第1の汚物処理装置の実施形態1では、第1蓋を起立状態にしたことに基づいて、制御部によって脱臭装置の吸気部、及び送風部の動作が開始される。しかし、これに限らず、第1蓋の近傍に人感センサ等を設け、第1蓋を起立状態にする前から脱臭装置の吸気部、及び送風部の動作を開始してもよい。この際、第1蓋を起立状態にした直後と、第1蓋を起立状態にした後、所定の時間が経過した後とで、吸気部、及び送風部の動作する勢いを変化させてもよい。
(7)第1の汚物処理装置の実施形態1では、脱臭部が吸気部の他端面を覆うように配置されている。しかし、これに限らず、脱臭部を吸気部の一端面を覆うように配置してもよい。
(8)第1の汚物処理装置の実施形態3では、投入部に水封部を設けている。しかし、これに限らず、第1蓋において、投入部の投入口が当接する部分にパッキンを設けてもよい。
(9)第1の汚物処理装置の実施形態2では、脱臭装置が消臭剤と芳香剤とを有している。しかし、これに限らず、脱臭装置が消臭剤及び芳香剤のいずれか一方のみを有している構成でもよい。
The first waste disposal apparatus is not limited to the first to third embodiments described with reference to the above description and the drawings. For example, the following embodiments are also included in the technical scope of the first waste disposal apparatus.
(1) In Embodiment 1 of the first waste disposal apparatus, the deodorizing apparatus has a blower. However, the present invention is not limited to this, and a ventilation path communicating with the second connection port may be provided from the other end face of the intake section with a deodorizing section interposed. Further, a restricting portion is provided in the air passage to restrict air from flowing from the second connection port toward the intake port, and not to restrict air from flowing from the intake port to the second connection port. An exhaust port may be provided between the deodorizing section.
(2) In Embodiment 1 of the first waste disposal apparatus, the deodorizing apparatus has a blower. However, the configuration is not limited to this, and a configuration in which the blower is removed from the configuration of the first embodiment may be adopted.
(3) In Embodiment 1 of the first waste disposal apparatus, the deodorizing apparatus has a blower. However, the present invention is not limited to this, and a third connection port may be formed in the input section, and the third connection port may be connected to one end surface of the blower section by a blower path to communicate with each other.
(4) In Embodiment 1 of the first waste disposal apparatus, one end of the second ventilation path communicates with the first ventilation path. However, the present invention is not limited to this, and one end of the second ventilation path may be connected to the input section, and the other end may be connected to the separation section.
(5) In the first embodiment of the first waste disposal apparatus, the third ventilation path is provided with an intake section. However, the invention is not limited thereto, and a deodorizing section may be provided instead of the intake section, and the intake section and the deodorizing section may be used in combination.
(6) In Embodiment 1 of the first waste disposal apparatus, based on the fact that the first lid is in the upright state, the control unit starts the operation of the suction unit and the blower unit of the deodorization device. However, the present invention is not limited to this, and a human sensor or the like may be provided near the first lid, and the operations of the air intake unit and the air blowing unit of the deodorizing device may be started before the first lid is raised. At this time, the momentum at which the suction unit and the air blowing unit operate may be changed between immediately after the first lid is raised and after a predetermined time has elapsed after the first lid is raised. .
(7) In Embodiment 1 of the first waste disposal apparatus, the deodorizing section is disposed so as to cover the other end surface of the suction section. However, the present invention is not limited to this, and the deodorizing section may be arranged so as to cover one end surface of the intake section.
(8) In Embodiment 3 of the first waste disposal apparatus, the water sealing section is provided in the charging section. However, the present invention is not limited to this, and a packing may be provided in a portion of the first lid where the charging port of the charging unit contacts.
(9) In Embodiment 2 of the first waste disposal apparatus, the deodorizing apparatus has a deodorant and an aromatic. However, the configuration is not limited to this, and the deodorizing device may have only one of the deodorant and the fragrance.
 第2の汚物処理装置は上記記述及び図面によって説明した実施形態4に限定されるものではなく、例えば次のような実施形態でもよい。
(1)第2の汚物処理装置の実施形態4では、洗浄モードの際、第2開閉弁を閉じた状態にして、分解槽を除いた処理部に湯を貯留している。しかし、これに限らず、分解槽の下流側の排水路と、固形分排出部の基端部とに第3開閉弁及び第4開閉弁を設け、洗浄モードの際、第1開閉弁及び第2開閉弁を開いた状態にし、第3開閉弁及び第4開閉弁を閉じた状態にし、全ての処理部に湯を貯留してもよい。
(2)第2の汚物処理装置の実施形態4では、ヒーターが全ての処理部に設けられている。しかし、これに限らず、排出路や排水路等にヒーターを設けてもよい。
(3)第2の汚物処理装置の実施形態4では、洗浄モードの際、分離部のモータ以外のモータを正方向と逆方向とに交互に駆動させている。しかし、これに限らず、全ての処理部のモータを一方向に駆動させつつ、駆動速度を周期的に変化させてもよい。
(4)第2の汚物処理装置の実施形態4では、洗浄モードの際、全ての処理部を駆動させつつ、吐出部から湯を吐出している。しかし、これに限らず、洗浄モードの際、全ての処理部を駆動させつつ、吐出部から水を吐出し、吐出された水をヒーターで加熱してもよい。
The second waste disposal apparatus is not limited to the fourth embodiment described with reference to the above description and the drawings. For example, the second embodiment may be as follows.
(1) In Embodiment 4 of the second waste disposal apparatus, in the cleaning mode, the second open / close valve is closed, and hot water is stored in the processing unit except for the decomposition tank. However, the present invention is not limited to this, and a third on-off valve and a fourth on-off valve are provided on the drainage channel on the downstream side of the decomposition tank and on the base end of the solids discharge unit. Hot water may be stored in all of the processing units by setting the second on-off valve to an open state and closing the third on-off valve and the fourth on-off valve.
(2) In Embodiment 4 of the second waste disposal apparatus, heaters are provided in all processing units. However, the present invention is not limited to this, and a heater may be provided in a discharge channel, a drain channel, or the like.
(3) In Embodiment 4 of the second waste disposal apparatus, in the cleaning mode, motors other than the motor of the separation unit are alternately driven in the forward direction and the reverse direction. However, the present invention is not limited to this, and the driving speed may be changed periodically while driving the motors of all the processing units in one direction.
(4) In Embodiment 4 of the second waste disposal apparatus, in the cleaning mode, hot water is discharged from the discharge unit while driving all the processing units. However, the present invention is not limited to this. In the cleaning mode, water may be discharged from the discharge unit while all the processing units are driven, and the discharged water may be heated by the heater.
 第3の汚物処理装置は上記記述及び図面によって説明した実施形態5に限定されるものではなく、例えば次のような実施形態でもよい。
(1)第3の汚物処理装置の実施形態5では、第1開閉弁の上流側に第1手動開閉弁が設けられ、第2開閉弁の上流側に第2手動開閉弁が設けられている。しかし、これに限らず、第1開閉弁の下流側に第1手動開閉弁を設け、第2開閉弁の下流側に第2手動開閉弁を設けてもよい。
The third waste disposal apparatus is not limited to the fifth embodiment described with reference to the above description and the drawings, and may be, for example, the following embodiment.
(1) In Embodiment 5 of the third waste disposal apparatus, the first manual open / close valve is provided upstream of the first open / close valve, and the second manual open / close valve is provided upstream of the second open / close valve. . However, the present invention is not limited to this, and a first manual open / close valve may be provided downstream of the first open / close valve, and a second manual open / close valve may be provided downstream of the second open / close valve.
 第1の汚物処理装置、第2の汚物処理装置及び第3の汚物処理装置は上記記述及び図面によって説明した実施形態1、実施形態4、及び実施形態5に限定されるものではなく、例えば次のような実施形態でもよい。
(1)第1の汚物処理装置の実施形態1、第2の汚物処理装置の実施形態4、及び第3の汚物処理装置の実施形態5では、分解剤として、CaCl2を用いている。しかし、これに限らず、CaやMg等の2価の金属塩を含んだ他の成分、例えば、酢酸カルシウム、塩化マグネシウム、硝酸マグネシウムの水溶性のアルカリ土金属塩等を含んでいてもよい。
(2)第1の汚物処理装置の実施形態1、第2の汚物処理装置の実施形態4、及び第3の汚物処理装置の実施形態5では、破砕部としてディスポーザーを例示している。しかし、これに限らず、グラインダーポンプ等の他の装置を破砕部として用いてもよい。
(3)分解剤は、固体であってもよく、液体であってもよい。分解剤が液体である場合、分解剤を貯蔵する分解剤貯蔵タンクと、分解剤貯蔵タンクから分解剤を取り出して投入路に向けて送り出すポンプとを有する分解剤投入装置を用いる。
(4)第1の汚物処理装置の実施形態1、第2の汚物処理装置の実施形態4、及び第3の汚物処理装置の実施形態5では、吐出部が投入部に設けられている。しかし、これに限らず、吐出部を希釈槽に設けてもよい。
(5)第1の汚物処理装置の実施形態1、第2の汚物処理装置の実施形態4、及び第3の汚物処理装置の実施形態5では、分離部を設けている。しかし、下水管に希釈物をそのまま流してもよい場合、希釈物から固形分を分離する必要がないため、分離部を設けなくてもよい。
(6)第1の汚物処理装置の実施形態1、第2の汚物処理装置の実施形態4、及び第3の汚物処理装置の実施形態5では、制御部は破砕部のモータの第1負荷の大きさに基づいて投入された汚物の量を推定している。しかし、これに限らず、投入部に投入された汚物の数を計数する計数部を設け、制御部は計数部からの信号に基づいて投入された汚物の量を推定してもよい。
(7)第1の汚物処理装置の実施形態1、第2の汚物処理装置の実施形態4、及び第3の汚物処理装置の実施形態5では、希釈槽の側面、及び分離部の側面に点検口が形成されている。しかし、これに限らず、希釈槽の上面、及び分離部の上面に点検口を設けてもよい。
The first sewage treatment apparatus, the second sewage treatment apparatus, and the third sewage treatment apparatus are not limited to the first, fourth, and fifth embodiments described above and illustrated in the drawings. Such an embodiment may be used.
(1) In Embodiment 1 of the first waste disposal apparatus, Embodiment 4 of the second waste disposal apparatus, and Embodiment 5 of the third waste disposal apparatus, CaCl 2 is used as a decomposing agent. However, the present invention is not limited to this, and may include other components including a divalent metal salt such as Ca and Mg, for example, a water-soluble alkaline earth metal salt of calcium acetate, magnesium chloride, and magnesium nitrate.
(2) In Embodiment 1 of the first waste disposal apparatus, Embodiment 4 of the second waste disposal apparatus, and Embodiment 5 of the third waste disposal apparatus, a disposer is illustrated as the crushing unit. However, the invention is not limited to this, and another device such as a grinder pump may be used as the crushing unit.
(3) The decomposing agent may be solid or liquid. When the decomposing agent is a liquid, a decomposing agent storage device that has a decomposing agent storage tank for storing the decomposing agent and a pump that takes out the decomposing agent from the decomposing agent storage tank and feeds the decomposed agent toward an input path is used.
(4) In Embodiment 1 of the first waste disposal apparatus, Embodiment 4 of the second waste disposal apparatus, and Embodiment 5 of the third waste disposal apparatus, the discharge unit is provided in the input unit. However, the present invention is not limited to this, and the discharge unit may be provided in the dilution tank.
(5) In Embodiment 1 of the first waste disposal apparatus, Embodiment 4 of the second waste disposal apparatus, and Embodiment 5 of the third waste disposal apparatus, a separation unit is provided. However, in the case where the diluent may be allowed to flow through the sewer pipe as it is, there is no need to separate the solid content from the diluent, so that a separation unit may not be provided.
(6) In Embodiment 1 of the first waste disposal apparatus, Embodiment 4 of the second waste disposal apparatus, and Embodiment 5 of the third waste disposal apparatus, the control unit controls the first load of the motor of the crushing unit. The amount of waste input is estimated based on the size. However, the present invention is not limited to this, and a counting unit that counts the number of filths input to the input unit may be provided, and the control unit may estimate the amount of the input filth based on a signal from the counting unit.
(7) In Embodiment 1 of the first waste disposal apparatus, Embodiment 4 of the second waste disposal apparatus, and Embodiment 5 of the third waste disposal apparatus, inspection is performed on the side of the dilution tank and the side of the separation unit. The mouth is formed. However, the present invention is not limited thereto, and an inspection port may be provided on the upper surface of the dilution tank and the upper surface of the separation unit.
 第4の汚物処理装置は上記記述及び図面によって説明した実施形態6に限定されるものではなく、例えば次のような実施形態でもよい。
(1)第4の汚物処理装置の実施形態6では、酢酸カルシウムを含む処理剤を投入する第1処理剤投入部と、塩化カルシウムを含む処理剤を投入する第2処理剤投入部と、を処理剤投入部が有する形態を例示した。しかし、これに限らず、1つの処理剤投入部のみを有する形態であってもよい。この場合、1つの処理剤投入部は、酢酸カルシウムと、塩化カルシウムと、が予め混合された処理剤を投入するものであってもよいし、酢酸カルシウムのみを含む処理剤を投入するものであってもよい。
(2)第4の汚物処理装置の実施形態6では、処理部の運転状態に関する情報を取得する情報取得部としての制御部及び測定部を備える形態を例示した。しかし、本開示に係る汚物処理装置において、この構成は必須ではない。情報取得部を備える場合、取得する処理部の運転状態に関する情報としては、例示した負荷低減時間、及び各測定部によって測定した消費電流値に限定されず、例えば、モータの温度や回転数、振動周波数、処理部内部の水位や圧力等の数値や、これら数値に基づいて得られる呈色変化、異音や騒音等の数値以外の情報であってもよい。すなわち、情報取得部としては、これらの数値を直接的に測定した測定値を取得する形態であってもよいし、測定した数値等の情報に基づいて処理部の運転状態に関する情報を間接的に取得する形態であってもよい。
(3)第4の汚物処理装置の実施形態6では、記憶部に記憶された過去の運転状態に関する情報に基づいて判定部が処理部の状況を予測する形態を例示した。しかし、これは必須ではない。判定部が処理部の状況を予測する場合、その手法は例示した直線回帰による回帰分析に限定されず、他の線形回帰や非線形回帰による回帰分析等、他の手法によるものであってもよい。
(4)第4の汚物処理装置の実施形態6では、判定部が被処理物の状態を判定する形態として、計測部の計測結果に基づいて判定する形態、及び測定部の測定結果に基づいて判定する形態をそれぞれ例示した。しかし、これに限らず、いずれか一方の結果に基づいて判定する形態であってもよいし、他の事項に基づいて判定する形態であってもよい。
(5)第4の汚物処理装置の実施形態6では、被処理物である紙おむつの状態に対して処理剤投入部から投入された処理剤の量の不足を制御部が検出したときに、処理部の運転を停止する制御を実行する形態を例示した。しかし、本開示に係る汚物処理装置においては必須ではなく、例えば、単に報知部によって報知する形態等であってもよい。
The fourth waste disposal apparatus is not limited to the sixth embodiment described with reference to the above description and drawings, and may be, for example, the following embodiment.
(1) In Embodiment 6 of the fourth waste disposal apparatus, the first processing agent input section for inputting the processing agent containing calcium acetate and the second processing agent input section for inputting the processing agent containing calcium chloride are provided. The form which the treatment agent introduction part has is illustrated. However, the present invention is not limited to this, and may be a form having only one treatment agent charging section. In this case, one treatment agent charging section may charge a treatment agent in which calcium acetate and calcium chloride are mixed in advance, or may charge a treatment agent containing only calcium acetate. You may.
(2) In the sixth embodiment of the fourth waste disposal apparatus, an example was described in which the control unit and the measurement unit as an information acquisition unit for acquiring information on the operation state of the processing unit were provided. However, in the waste disposal apparatus according to the present disclosure, this configuration is not essential. When the information acquisition unit is provided, the information on the operation state of the processing unit to be acquired is not limited to the exemplified load reduction time, and the current consumption value measured by each measurement unit. Numerical values such as the frequency, the water level and the pressure inside the processing unit, and information other than the numerical values such as color change, abnormal noise and noise obtained based on these numerical values may be used. That is, the information acquisition unit may be a form of directly acquiring a measurement value obtained by directly measuring these numerical values, or may indirectly acquire information on the operating state of the processing unit based on information such as the measured numerical values. The acquisition form may be used.
(3) In the sixth embodiment of the fourth waste disposal apparatus, the form in which the determination unit predicts the state of the processing unit based on the information on the past operation state stored in the storage unit has been exemplified. However, this is not required. When the determination unit predicts the state of the processing unit, the method is not limited to the linear regression analysis described above, but may be another method, such as another linear regression or a non-linear regression analysis.
(4) In the sixth embodiment of the fourth filth disposal apparatus, the determination unit determines the state of the object to be processed based on the measurement result of the measurement unit, and based on the measurement result of the measurement unit. Each of the determination modes has been exemplified. However, the present invention is not limited to this, and the determination may be made based on one of the results, or the determination may be made based on another matter.
(5) In the sixth embodiment of the waste disposal apparatus, when the control unit detects that the amount of the processing agent supplied from the processing agent input unit is insufficient for the state of the disposable diaper to be processed, The form in which the control for stopping the operation of the unit is executed has been exemplified. However, it is not essential in the waste disposal apparatus according to the present disclosure.
 第5の汚物処理装置は上記記述及び図面によって説明した実施形態6に限定されるものではなく、例えば次のような実施形態でもよい。
(1)第5の汚物処理装置の実施形態6では、処理剤投入部を備え、処理剤が制御部の制御によって投入される形態を例示した。しかし、これは必須の構成ではなく、作業者によって手動にて投入される形態であってもよい。
(2)第5の汚物処理装置の実施形態6では、処理剤投入部を備え、この処理剤投入部が酢酸カルシウムを含む処理剤を投入する第1処理剤投入部と、塩化カルシウムを含む処理剤を投入する第2処理剤投入部と、を有する形態を例示した。これに対して、処理剤投入部を1つ有する形態でもよく、3つ以上を有する形態であってもよい。1つの処理剤投入部のみを有する場合には、例えば、酢酸カルシウム、塩化カルシウム等の異なる種類の成分が予め混合された処理剤を投入するものであってもよいし、酢酸カルシウム等の1つの成分のみを含む処理剤を投入するものであってもよい。
(3)第5の汚物処理装置の実施形態6では、判定部が被処理物の状態を判定する形態を例示した。しかし、本開示に係る汚物処理装置においてこれは必須ではない。判定部が被処理物の状態を判定する場合には、例示した計測部の計測結果に基づいて判定する形態、及び測定部の測定結果に基づいて判定する形態に限定されず、いずれか一方の結果に基づいて判定する形態であってもよいし、他の事項に基づいて判定する形態であってもよい。
(4)第5の汚物処理装置の実施形態6では、被処理物である紙おむつの状態に対して処理剤投入部から投入された処理剤の量の不足を制御部が検出したときに、処理部の運転を停止する制御を実行する形態を例示した。しかし、本開示に係る汚物処理装置においては、このような制御部を備えることは必須ではない。
(5)第5の汚物処理装置の実施形態6では、処理部の運転状態に関する情報として、制御部が計測した破砕部、ミキサ、希釈槽、及び分離部における処理時の負荷低減時間、及び破砕部、ミキサ、希釈槽、及び分離部の各モータの消費電流を各測定部によって測定した値を例示した。しかし、これらに限定されず、例えば、モータの温度や回転数、振動周波数、処理部内部の水位や圧力等の数値や、これら数値に基づいて得られる呈色変化、異音や騒音等の数値以外の情報であってもよい。すなわち、情報取得部としては、これらの数値を直接的に測定した測定値を取得する形態であってもよいし、測定した数値等の情報に基づいて処理部の運転状態に関する情報を間接的に取得する形態であってもよい。
(6)第5の汚物処理装置の実施形態6では、判定部が処理部の状況を予測する手法として、直線回帰による回帰分析を例示した。しかし、これに限らず、他の線形回帰や非線形回帰による回帰分析等、他の手法によるものであってもよい。
The fifth waste disposal apparatus is not limited to the sixth embodiment described with reference to the above description and drawings, and may be, for example, the following embodiment.
(1) In the sixth embodiment of the fifth filth disposal apparatus, the form in which the treatment agent introduction section is provided and the treatment agent is introduced under the control of the control section is exemplified. However, this is not an essential configuration, and may be a form that is manually input by an operator.
(2) In the sixth embodiment of the fifth filth disposal apparatus, a processing agent input section is provided, the processing agent input section inputs a processing agent including calcium acetate, and a processing including calcium chloride. And a second treatment agent introduction section for introducing the agent. On the other hand, a form having one treatment agent charging section or a form having three or more treatment agent charging sections may be used. In the case of having only one treatment agent introduction part, for example, a treatment agent in which different kinds of components such as calcium acetate and calcium chloride are mixed in advance may be introduced, or one treatment agent such as calcium acetate or the like may be introduced. A treatment agent containing only components may be added.
(3) In the sixth embodiment of the fifth filth disposal apparatus, an example is described in which the determination unit determines the state of the workpiece. However, this is not essential in the waste disposal apparatus according to the present disclosure. When the determination unit determines the state of the object to be processed, the determination is not limited to the form based on the measurement result of the exemplified measurement unit and the form based on the measurement result of the measurement unit. The determination may be based on the result, or the determination may be based on other items.
(4) In the sixth embodiment of the waste disposal apparatus, when the control unit detects that the amount of the processing agent supplied from the processing agent input unit is insufficient for the state of the disposable diaper to be processed, The form in which the control for stopping the operation of the unit is executed has been exemplified. However, it is not essential to provide such a control unit in the waste disposal apparatus according to the present disclosure.
(5) In the sixth embodiment of the fifth waste disposal apparatus, as the information on the operation state of the processing unit, the load reduction time during the processing in the crushing unit, the mixer, the dilution tank, and the separation unit measured by the control unit, and the crushing The values obtained by measuring the current consumption of each motor of the section, the mixer, the dilution tank, and the separation section by each measurement section are illustrated. However, the present invention is not limited to these. For example, numerical values such as motor temperature, rotation speed, vibration frequency, water level and pressure inside the processing unit, and numerical values such as color change, abnormal noise and noise obtained based on these numerical values, Other information may be used. That is, the information acquisition unit may be a form of directly acquiring a measurement value obtained by directly measuring these numerical values, or may indirectly acquire information on the operating state of the processing unit based on information such as the measured numerical values. The acquisition form may be used.
(6) In the sixth embodiment of the fifth filth disposal apparatus, a regression analysis by linear regression is exemplified as a method in which the determination unit predicts the state of the processing unit. However, the present invention is not limited to this, and other methods such as regression analysis using linear regression or non-linear regression may be used.
 第4の汚物処理装置及び第5の汚物処理装置は上記記述及び図面によって説明した実施形態6に限定されるものではなく、例えば次のような実施形態でもよい。
(1)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、被処理物として紙おむつを例示した。しかし、これに限らず、被処理部として生理用品、ペット用シートやペット用砂等、他の物であってもよい。
(2)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、処理部として、破砕部、ミキサ、希釈槽、及び分離部を有して構成されている形態を例示した。しかし、処理部の構成は実施形態の形態に限定されない。例えば、破砕部、ミキサ、希釈槽、及び分離部のうちの1つ以上を設けない構成等、実施形態で説明した処理部の一部を有さない構成であってもよいし、第2ミキサ等の他の処理部を更に有する構成であってもよいし、ミキサ及び希釈槽の2つの処理部に替えて混合工程及び希釈工程を行う1つの処理部を有する構成等、複数の工程を1つに統合した処理部を有する構成であってもよい。
(3)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、給水部が投入部に設けられている形態を例示した。しかし、これに限らず、給水部は、投入部以外、例えば、破砕部、ミキサ、希釈槽、分離部等の処理部に設けられていてもよいし、投入部とミキサ、破砕部とミキサと希釈槽等、複数箇所に設けられていてもよい。
(4)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、給水部が水及び湯の少なくとも一方を供給する形態を例示した。しかし、これに限らず、水のみであってもよい。
(5)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では報知部を備える形態を例示した。しかし、本開示に係る汚物処理装置では必須の構成ではない。報知部を備える場合には、例示した文字や図形等を表示する表示器に限定されず、音や音声を発するブザーやスピーカー等であってもよいし、異なる種類の報知部を組み合わせた形態であってもよい。
(6)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では記憶部を備える形態を例示した。しかし、本開示に係る汚物処理装置では必須の構成ではない。
(7)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では送信部を備える形態を例示した。しかし、本開示に係る汚物処理装置では必須の構成ではない。
(8)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、処理剤として、酢酸カルシウムを含む処理剤及び塩化カルシウムを含む処理剤の2種類の処理剤を用いる形態を例示した。しかし、これに限らず、CaやMg等の2価の金属塩を含んだ他の薬剤を用いてもよく、塩化マグネシウム、硝酸マグネシウムの水溶性のアルカリ土類金属塩等を含むものであってもよい。処理剤として酢酸カルシウムを用いる場合には、例示した通常運転時には塩化カルシウムを含む処理剤と併用し、洗浄モード時には酢酸カルシウムを含む処理剤のみ用いる方法のみならず、装置の通常運転時から酢酸カルシウムを含む処理剤のみを用いてもよいし、酢酸カルシウムを含む処理剤を複数回の通常運転毎に1回投入する等の使用方法としてもよい。
(9)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、処理剤として固体の処理剤を例示した。しかし、これに限らず、液体であってもよい。処理剤が液体である場合、処理剤供給部としては、公知の定量ポンプ等を用いることができる。
(10)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、判定部に予測された処理部の状況が所定の状況、すなわち、測定部によって測定した運転状態に関する情報としての消費電流値が所定値を超える場合に、処理部の洗浄運転を実行する形態を例示した。しかし、本開示に係る汚物処理装置においては必須ではない。
(11)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、洗浄運転としての洗浄モードを行った後に判定部が処理部の状況を再判定する形態を例示した。しかし、本開示に係る汚物処理装置においては必須ではない。
(12)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、投入部から投入された被処理物の個数を計測する計測部を備える形態を例示した。しかし、本開示に係る汚物処理装置において、計測部を備えることは必須ではない。計測部を備える場合、計測部の形態としては、例示した光電センサに限らず、例えば、レーザセンサ、画像センサ等の他のセンサである形態等であってもよい。計測部の計測対象としては、被処理物の個数のみならず、大きさや重量等であってもよい。
(13)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、計測部が被処理物の個数を計測する形態を例示した。しかし、これに限らず、計測部が被処理物を計測する形態としては、被処理物の重量を計測する形態や、駆動部としてのモータの消費電流値を計測する形態等の他の形態であってもよい。この場合、計測部の配置される位置としては、例示した投入部の投入口のみならず、破砕部、シュート、ミキサ等の装置の他の位置であってもよい。
(14)第4の汚物処理装置及び第5の汚物処理装置の実施形態6では、制御部によって、制御部が決定した投入量の処理剤を処理剤投入部から投入させる形態を例示した。しかし、これは必須ではない。例えば、制御部が決定した処理剤の投入量を報知部によって報知させることで、作業者が手動で処理剤を投入する形態であってもよい。
The fourth waste disposal apparatus and the fifth waste disposal apparatus are not limited to the sixth embodiment described above with reference to the drawings, but may be, for example, the following embodiments.
(1) In Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, a disposable diaper was illustrated as an object to be treated. However, the present invention is not limited to this, and other objects such as sanitary products, pet sheets, pet sand, and the like may be used as the processing target.
(2) In the sixth embodiment of the fourth and fifth waste disposal apparatuses, an example in which the processing section includes a crushing section, a mixer, a dilution tank, and a separation section has been described. However, the configuration of the processing unit is not limited to the embodiment. For example, a configuration that does not include a part of the processing unit described in the embodiment, such as a configuration that does not include one or more of a crushing unit, a mixer, a dilution tank, and a separation unit, or a second mixer Or a configuration having one processing unit for performing a mixing step and a dilution step instead of the two processing units of the mixer and the dilution tank. It may be configured to have a processing unit integrated into one.
(3) In Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, the form in which the water supply section is provided in the input section has been exemplified. However, not limited to this, the water supply unit may be provided in a processing unit such as a crushing unit, a mixer, a dilution tank, and a separation unit other than the charging unit, or a charging unit and a mixer, and a crushing unit and a mixer. It may be provided at a plurality of places such as a dilution tank.
(4) In Embodiment 6 of the fourth and fifth waste disposal apparatuses, an example in which the water supply unit supplies at least one of water and hot water has been described. However, the present invention is not limited to this, and only water may be used.
(5) In Embodiment 6 of the fourth and fifth waste disposal apparatuses, the form provided with the notification unit was exemplified. However, this is not an essential configuration in the waste disposal apparatus according to the present disclosure. When the notification unit is provided, the display unit is not limited to the display device that displays the characters or graphics as exemplified, but may be a buzzer or a speaker that emits a sound or a voice, or may be a combination of different types of notification units. There may be.
(6) In Embodiment 6 of the fourth and fifth waste disposal apparatuses, the form provided with the storage unit was exemplified. However, this is not an essential configuration in the waste disposal apparatus according to the present disclosure.
(7) The sixth embodiment of the fourth and fifth waste disposal apparatuses has exemplified the form including the transmission unit. However, this is not an essential configuration in the waste disposal apparatus according to the present disclosure.
(8) In Embodiment 6 of the fourth filth treatment apparatus and the fifth filth treatment apparatus, an example in which two types of treatment agents, that is, a treatment agent containing calcium acetate and a treatment agent containing calcium chloride, are used as treatment agents did. However, the present invention is not limited to this, and other chemicals containing divalent metal salts such as Ca and Mg may be used, and may contain magnesium chloride, water-soluble alkaline earth metal salts of magnesium nitrate, and the like. Is also good. When calcium acetate is used as the treatment agent, not only the method using only the treatment agent containing calcium acetate in the washing mode in combination with the treatment agent containing calcium chloride in the illustrated normal operation, but also the method using calcium acetate during the normal operation of the apparatus May be used alone, or a treatment method containing calcium acetate may be added once for each of a plurality of normal operations.
(9) In Embodiment 6 of the fourth and fifth waste disposal apparatuses, a solid treatment agent is exemplified as the treatment agent. However, the present invention is not limited to this, and may be a liquid. When the treatment agent is a liquid, a known metering pump or the like can be used as the treatment agent supply unit.
(10) In Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, the state of the processing unit predicted by the determination unit is a predetermined state, that is, information on the operating state measured by the measurement unit. The example in which the cleaning operation of the processing unit is executed when the current consumption value exceeds the predetermined value has been described. However, this is not essential in the waste disposal apparatus according to the present disclosure.
(11) In Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, an example in which the determination unit re-determines the status of the processing unit after performing the cleaning mode as the cleaning operation has been described. However, this is not essential in the waste disposal apparatus according to the present disclosure.
(12) In Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, an example in which a measuring unit that measures the number of objects to be treated input from the input unit is illustrated. However, it is not essential for the waste disposal apparatus according to the present disclosure to include the measuring unit. When a measurement unit is provided, the form of the measurement unit is not limited to the illustrated photoelectric sensor, but may be another sensor such as a laser sensor or an image sensor. The measurement target of the measurement unit may be not only the number of the objects to be processed, but also the size, weight, and the like.
(13) In Embodiment 6 of the fourth waste disposal apparatus and the fifth waste disposal apparatus, the form in which the measuring unit measures the number of the objects to be treated has been described. However, the present invention is not limited to this. Examples of the form in which the measuring unit measures the object to be processed include other forms such as a form in which the weight of the work is measured and a mode in which the current consumption value of a motor as a driving unit is measured. There may be. In this case, the position where the measuring unit is arranged may be not only the input port of the illustrated input unit but also another position of the crushing unit, the chute, the mixer, or the like.
(14) In the sixth embodiment of the fourth and fifth waste disposal apparatuses, the control unit exemplifies a mode in which the processing agent of the amount determined by the control unit is introduced from the processing agent introduction unit. However, this is not required. For example, a mode in which the operator manually inputs the processing agent by notifying the input amount of the processing agent determined by the control unit by the notification unit may be employed.

Claims (28)

  1.  水分を吸収保持可能なポリマーを有する汚物を投入する投入部と、
     前記汚物を破砕して破砕物にする破砕部と、
     前記投入部の接続口に接続され、前記汚物及び前記破砕物の少なくともいずれか一方から生じる臭気を脱臭する脱臭装置と、
     を備える汚物処理装置。
    An input section for inputting waste having a polymer capable of absorbing and retaining moisture,
    A crushing unit that crushes the filth to make crushed material,
    A deodorization device connected to the connection port of the charging section, for deodorizing an odor generated from at least one of the waste and the crushed material,
    Waste treatment device comprising:
  2.  前記破砕部の下流側に連通し、前記破砕物を水で希釈して希釈物にする希釈槽と、
     一端が前記接続口よりも下流側に接続され、他端が前記希釈槽に接続された第1通気路と、
     を備えている請求項1に記載の汚物処理装置。
    A dilution tank that communicates with the downstream side of the crushing unit and dilutes the crushed material with water to make a diluted material;
    A first ventilation path having one end connected to the downstream side of the connection port and the other end connected to the dilution tank;
    The waste disposal apparatus according to claim 1, comprising:
  3.  前記希釈槽の下流側に接続され、前記希釈物から固形分を分離する分離部と、
     一端が前記投入部、及び前記第1通気路の少なくともいずれか一方に接続され、他端が前記分離部に接続された第2通気路と、
     を備えている請求項2に記載の汚物処理装置。
    A separation unit connected to the downstream side of the dilution tank and separating a solid content from the diluent,
    A second ventilation path having one end connected to at least one of the input section and the first ventilation path, and the other end connected to the separation section;
    The waste disposal apparatus according to claim 2, comprising:
  4.  前記投入部を閉鎖する蓋と、
     前記希釈槽内及び前記分離部内の少なくとも一方の負圧を解消する負圧解消部と、
     を備えている請求項3に記載の汚物処理装置。
    A lid for closing the input section,
    A negative pressure eliminating unit that eliminates at least one negative pressure in the dilution tank and the separation unit;
    The waste disposal apparatus according to claim 3, comprising:
  5.  前記分離部は、前記希釈物から分離した前記固形分を排出する固形分排出部を有し、
     一端が前記投入部に接続され、他端が前記固形分排出部に接続された第3通気路、
     を備えている請求項3から請求項4までのいずれか一項に記載の汚物処理装置。
    The separation unit has a solid content discharge unit that discharges the solid content separated from the diluent,
    A third ventilation path having one end connected to the input section and the other end connected to the solids discharge section;
    The waste disposal apparatus according to any one of claims 3 to 4, comprising:
  6.  前記脱臭装置は、前記投入部から吸気する吸気部、及び前記投入部に送風する送風部を有している請求項1から5までのいずれか1項に記載の汚物処理装置。 The waste disposal apparatus according to any one of claims 1 to 5, wherein the deodorizing device includes an air suction unit that sucks air from the charging unit and a blowing unit that blows air to the charging unit.
  7.  前記脱臭装置は、臭気を消す消臭剤、及び芳香を生じる芳香剤の少なくともいずれか一方を有している請求項1から6までのいずれか1項に記載の汚物処理装置。 The waste disposal apparatus according to any one of claims 1 to 6, wherein the deodorizing device includes at least one of a deodorant for eliminating odors and a fragrance for generating fragrance.
  8.  水分を吸収保持可能なポリマーを有する汚物を投入する投入部と、
     前記汚物を分離処理する処理部と、
     を備えた汚物処理装置であって、
     前記汚物を分離処理する処理モードと、前記処理部を洗浄する洗浄モードとを選択的に実行することができ、
     前記洗浄モードの際、水及び湯の少なくともいずれか一方を吐出する吐出部を備えている汚物処理装置。
    An input section for inputting waste having a polymer capable of absorbing and retaining moisture,
    A processing unit that separates the waste,
    A waste disposal apparatus comprising:
    A processing mode for separating the filth and a cleaning mode for cleaning the processing unit can be selectively executed,
    A waste disposal apparatus including a discharge unit that discharges at least one of water and hot water in the cleaning mode.
  9.  前記湯の温度は40℃から90℃である請求項8に記載の汚物処理装置。 汚 The waste disposal apparatus according to claim 8, wherein the temperature of the hot water is from 40 ° C to 90 ° C.
  10.  前記処理部の下流側に開閉弁を備え、前記洗浄モードの際に前記開閉弁を閉弁して前記処理部に水及び湯の少なくともいずれか一方を貯留する請求項8から請求項9までのいずれか一項に記載の汚物処理装置。 An on-off valve downstream of the processing unit, wherein the on-off valve is closed in the cleaning mode to store at least one of water and hot water in the processing unit. The waste disposal apparatus according to claim 1.
  11.  前記洗浄モードの際、前記処理部を駆動させつつ、前記吐出部から水及び湯の少なくともいずれか一方を吐出する請求項8から請求項10までのいずれか1項に記載の汚物処理装置。 The waste disposal apparatus according to any one of claims 8 to 10, wherein, in the cleaning mode, at least one of water and hot water is discharged from the discharge unit while driving the processing unit.
  12.  前記処理部に設けられ、前記処理部内の水及び湯の少なくともいずれか一方を加熱するヒーターを備えている請求項8から請求項11までのいずれか1項に記載の汚物処理装置。 The waste disposal apparatus according to any one of claims 8 to 11, further comprising a heater provided in the processing unit, the heater configured to heat at least one of water and hot water in the processing unit.
  13.  水分を吸収保持可能なポリマーを有する汚物を分離処理し、直列に接続された複数の処理部を備え、
     下流側の前記処理部が一回の処理で処理できる処理量が上流側の前記処理部が一回の処理で処理できる処理量以上である汚物処理装置。
    Separation treatment of dirt having a polymer capable of absorbing and holding moisture, comprising a plurality of processing units connected in series,
    A waste disposal apparatus in which the processing amount that can be processed by the downstream processing unit in a single process is equal to or greater than the processing amount that the upstream processing unit can process in a single process.
  14.  1つ及び複数の少なくともいずれか一方の前記処理部で構成されるグループを複数構成し、複数の前記グループの処理時間がほぼ等しいか、及び上流側の前記グループよりも下流側の前記グループの処理時間が短いかいずれか一方の請求項13に記載の汚物処理装置。 A plurality of groups each including one and / or a plurality of the processing units are configured, and processing times of the plurality of groups are substantially equal, and processing of the group on the downstream side of the group on the upstream side is performed. 14. The waste disposal apparatus according to claim 13, wherein the time is short.
  15.  複数の前記グループ同士を接続する接続部に開閉弁が設けられている請求項14に記載の汚物処理装置。 The waste disposal apparatus according to claim 14, wherein an on-off valve is provided at a connection portion connecting the plurality of groups.
  16.  複数の前記グループ毎に着脱自在である請求項15に記載の汚物処理装置。 The waste disposal apparatus according to claim 15, wherein the waste disposal apparatus is detachable for each of the plurality of groups.
  17.  吸水性のポリマーを有した被処理物が投入される投入部と、
     前記ポリマーの吸水性能を抑制するための処理剤を用いて前記被処理物の処理を行う処理部と、
     前記投入部から投入された前記被処理物の状態を判定する判定部を有するとともに、前記判定部によって判定した前記被処理物の状態に基づいて、前記処理剤の投入量を決定する制御部と、
    を備えている汚物処理装置。
    An input section into which an object to be processed having a water-absorbing polymer is input,
    A processing unit that performs processing of the object to be processed using a processing agent for suppressing the water absorption performance of the polymer,
    A control unit that has a determination unit that determines the state of the processing object input from the input unit, and that determines the input amount of the processing agent based on the state of the processing object determined by the determination unit. ,
    Waste treatment equipment provided with.
  18.  前記処理部に前記処理剤を投入する処理剤投入部と、
     前記投入部から投入された前記被処理物の個数を計測する計測部と、
    を備えており、
     前記判定部は、前記計測部の計測結果に基づいて前記状態を判定し、
     前記制御部は、決定した投入量の前記処理剤を前記処理剤投入部から投入させる請求項17に記載の汚物処理装置。
    A treatment agent introduction unit for introducing the treatment agent into the treatment unit,
    A measuring unit that measures the number of the processing objects input from the input unit,
    With
    The determination unit determines the state based on the measurement result of the measurement unit,
    The waste disposal apparatus according to claim 17, wherein the control unit causes the determined amount of the processing agent to be input from the processing agent input unit.
  19.  前記制御部は、決定した前記投入量に対して、前記処理剤投入部が投入可能な前記処理剤の量の不足を検出したときには、前記処理部の運転を停止する請求項18に記載の汚物処理装置。 19. The filth according to claim 18, wherein the control unit stops the operation of the processing unit when the processing agent input unit detects a shortage of the amount of the processing agent that can be input for the determined input amount. Processing equipment.
  20.  稼働状況に関する情報を報知する報知部を備えている請求項17から請求項19までのいずれか一項に記載の汚物処理装置。 20. The waste disposal apparatus according to any one of claims 17 to 19, further comprising: a notifying unit that notifies information on an operation status.
  21.  前記稼働状況に関する情報を記憶する記憶部を備えている請求項20に記載の汚物処理装置。 21. The waste disposal apparatus according to claim 20, further comprising a storage unit configured to store information on the operation status.
  22.  前記稼働状況に関する情報を外部に送信する送信部を備えている請求項20から請求項21までのいずれか一項に記載の汚物処理装置。 The waste disposal apparatus according to any one of claims 20 to 21, further comprising a transmission unit configured to transmit the information on the operation status to the outside.
  23.  吸水性のポリマーを有した被処理物を前記ポリマーの吸水性能を抑制するための処理剤を用いて処理を行う処理部と、
     前記処理部の運転状態に関する情報を取得する情報取得部と、
     前記情報取得部によって取得された情報を記憶する記憶部と、
     前記情報取得部によって取得された情報に基づいて前記処理部の状況を判定する判定部と、
    を備えている汚物処理装置。
    A processing unit that performs processing using a processing agent for suppressing an object to be processed having a water-absorbing polymer to suppress the water-absorbing performance of the polymer,
    An information acquisition unit that acquires information about an operation state of the processing unit;
    A storage unit that stores information acquired by the information acquisition unit,
    A determining unit that determines the status of the processing unit based on the information acquired by the information acquiring unit,
    Waste treatment equipment provided with.
  24.  前記判定部は、前記記憶部に記憶された過去の前記情報に基づいて、前記処理部の状況を予測する請求項23に記載の汚物処理装置。 24. The waste disposal apparatus according to claim 23, wherein the determination unit predicts a state of the processing unit based on the past information stored in the storage unit.
  25.  前記判定部によって予測された前記処理部の状況が所定の状況である場合には、前記処理部を洗浄する洗浄運転を実行する請求項24に記載の汚物処理装置。 25. The waste disposal apparatus according to claim 24, wherein when the condition of the processing unit predicted by the determination unit is a predetermined condition, a cleaning operation for cleaning the processing unit is performed.
  26.  前記判定部は、前記洗浄運転を行った後に前記処理部の状況を再判定する請求項25に記載の汚物処理装置。 26. The waste disposal apparatus according to claim 25, wherein the determination unit re-determines a state of the processing unit after performing the cleaning operation.
  27.  前記情報を外部に送信する送信部を備えている請求項23から請求項26までのいずれか一項に記載の汚物処理装置。 The waste disposal apparatus according to any one of claims 23 to 26, further comprising: a transmission unit configured to transmit the information to the outside.
  28.  前記送信部は、複数の汚物処理装置の送信部から送信された各前記処理部の運転状態に関する情報を受信する外部の受信部に、前記情報を送信する請求項27に記載の汚物処理装置。 28. The filth disposal device according to claim 27, wherein the transmission unit transmits the information to an external reception unit that receives information on an operation state of each of the processing units transmitted from the transmission units of the plurality of filth disposal devices.
PCT/JP2019/037579 2018-09-28 2019-09-25 Waste treatment device WO2020067148A1 (en)

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JP2018185503A JP2020055132A (en) 2018-09-28 2018-09-28 Filth disposal device
JP2018-183080 2018-09-28
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JP2018183080A JP2020049446A (en) 2018-09-28 2018-09-28 Filth treatment system
JP2018183078A JP7177648B6 (en) 2018-09-28 2018-09-28 Sewage treatment equipment
JP2018-183078 2018-09-28
JP2018-185503 2018-09-28
JP2018-183079 2018-09-28
JP2018185510A JP2020054937A (en) 2018-09-28 2018-09-28 Filth disposal device
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JP2022155500A (en) * 2021-03-30 2022-10-13 ユニ・チャーム株式会社 Management device, management method, management program and management system
JP7494233B2 (en) 2021-03-30 2024-06-03 ユニ・チャーム株式会社 Management device, management method, management program, and management system

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