WO2021132570A1 - Ice supply device and ice making system - Google Patents

Ice supply device and ice making system Download PDF

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Publication number
WO2021132570A1
WO2021132570A1 PCT/JP2020/048749 JP2020048749W WO2021132570A1 WO 2021132570 A1 WO2021132570 A1 WO 2021132570A1 JP 2020048749 W JP2020048749 W JP 2020048749W WO 2021132570 A1 WO2021132570 A1 WO 2021132570A1
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WO
WIPO (PCT)
Prior art keywords
ice
water
sherbet
storage tank
temperature
Prior art date
Application number
PCT/JP2020/048749
Other languages
French (fr)
Japanese (ja)
Inventor
俊介 東矢
植野 武夫
Original Assignee
ダイキン工業株式会社
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 PCT/JP2020/035080 external-priority patent/WO2021131179A1/en
Application filed by ダイキン工業株式会社 filed Critical ダイキン工業株式会社
Priority to CN202080089740.0A priority Critical patent/CN114867975A/en
Priority to EP20905869.2A priority patent/EP4083542B1/en
Publication of WO2021132570A1 publication Critical patent/WO2021132570A1/en
Priority to US17/849,063 priority patent/US20220325933A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25CPRODUCING, WORKING OR HANDLING ICE
    • F25C1/00Producing ice
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B25/00Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
    • F25B25/005Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00 using primary and secondary systems
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B6/00Compression machines, plants or systems, with several condenser circuits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B13/00Compression machines, plants or systems, with reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/003Indoor unit with water as a heat sink or heat source
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B40/00Subcoolers, desuperheaters or superheaters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25CPRODUCING, WORKING OR HANDLING ICE
    • F25C2301/00Special arrangements or features for producing ice
    • F25C2301/002Producing ice slurries
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25CPRODUCING, WORKING OR HANDLING ICE
    • F25C2400/00Auxiliary features or devices for producing, working or handling ice
    • F25C2400/14Water supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25CPRODUCING, WORKING OR HANDLING ICE
    • F25C2700/00Sensing or detecting of parameters; Sensors therefor
    • F25C2700/14Temperature of water

Definitions

  • This disclosure relates to an ice supply device and an ice making system.
  • Sherbet ice produced from saltwater such as seawater may be used to refrigerate saltwater fish.
  • the sherbet ice produced by the ice maker is stored in an ice storage tank and pumped to the user at any time.
  • the temperature suitable for refrigeration differs depending on the fish species and size. If the saltwater fish is kept cold at a temperature lower than the temperature suitable for the saltwater fish to be kept cold, the body of the saltwater fish may freeze and its commercial value may be significantly impaired.
  • the salt concentration of the salt water mixed sherbet-shaped ice in the ice storage tank is adjusted by injecting fresh water into the ice storage tank, and the adjusted sherbet-shaped ice is stored. I'm taking it out of the tank.
  • the salt concentration of the sherbet ice is adjusted by injecting fresh water into the ice storage tank in which the produced sherbet ice is stored, so that a specific salt concentration can be adjusted. Only sherbet ice can be obtained. Therefore, when it is desired to refrigerate different types of saltwater fish, it is difficult to adjust the sherbet ice to a salt concentration suitable for the saltwater fish.
  • the ice supply device of the present disclosure is It is provided with an ice storage tank for storing sherbet ice, a supply path for taking out sherbet ice from the ice storage tank, and a water channel through which water flows, which joins the supply path.
  • a water channel through which water flows joins a supply path for taking out sherbet ice from an ice storage tank. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user.
  • the ice supply device of the above (1) further includes a pump arranged on the downstream side in the flow direction of sherbet ice from the confluence portion where the water flow path joins the supply path.
  • a pump arranged on the downstream side in the flow direction of the sherbet ice from the confluence portion, the sherbet ice and water can be flowed by one pump.
  • the flow rate adjusting valve provided in the water flow path and the front flow rate adjusting valve are controlled so that the salt concentration of sherbet ice after merging becomes a target value. It is desirable that the control unit is further provided. By controlling the flow rate adjusting valve provided in the water flow path by the control unit, the salt concentration of the sherbet ice after merging can be adjusted.
  • a first temperature sensor for detecting the temperature of the sherbet ice or a first for detecting the salt concentration of the sherbet ice is located downstream of the confluence in the flow direction of the sherbet ice. Equipped with a density sensor It is desirable that the control unit controls the flow rate adjusting valve so that the temperature detected by the first temperature sensor or the concentration detected by the first concentration sensor becomes a target value. By controlling the flow rate adjusting valve using the temperature or concentration detected by the first temperature sensor or the first concentration sensor, the salt concentration of the sherbet ice after merging can be adjusted.
  • a first temperature sensor for detecting the temperature of the sherbet ice is further provided on the downstream side in the flow direction of the sherbet ice from the confluence portion. It is desirable that the control unit calculates the salt concentration from the temperature detected by the first temperature sensor and controls the flow rate adjusting valve so that the calculated salt concentration becomes a target value. Since there is a correlation between the salt concentration of sherbet ice and the temperature, the salt concentration can be calculated from the detected temperature by detecting the temperature of the sherbet ice with the first temperature sensor. Then, the control unit adjusts the salt concentration of the sherbet ice after merging by controlling the flow rate adjusting valve so that the calculated salt concentration becomes the target value and adjusting the flow rate of the water merging into the supply path. be able to.
  • control unit controls the opening and / or opening time of the flow rate adjusting valve.
  • the control unit can adjust the flow rate of the water merging into the supply path by controlling the opening and / or opening time of the flow rate adjusting valve.
  • a second concentration sensor for detecting the salt concentration of sherbet ice in the ice storage tank is further provided. It is desirable that the control unit prohibits the operation of taking out the sherbet ice in the ice storage tank when the salt concentration detected by the second concentration sensor is not within the predetermined range. By prohibiting the operation of taking out the sherbet ice in the ice storage tank when the detected salt concentration is not within the predetermined range, it is possible to suppress the supply of the sherbet ice in an insufficient state to the user.
  • the second temperature sensor for detecting the temperature of the sherbet ice in the ice storage tank and the second temperature sensor.
  • the temperature of the medium to be cooled which was supplied to the ice storage tank before the operation of the ice making device and detected by the second temperature sensor, and stored in the ice storage tank after the operation of the ice making device was started and detected by the second temperature sensor.
  • the salinity calculation unit can calculate the salinity of the sherbet ice based on the temperature of the medium to be cooled before the operation and the temperature of the sherbet ice after the start of the operation detected by the second sensor.
  • the supply path is arranged in the ice storage tank and has an outlet for taking out sherbet ice in the ice storage tank. It is desirable that the outlet is arranged below the liquid level of sherbet ice in the ice storage tank by a predetermined distance.
  • High IPF Ice Packing Factor: ratio of the weight of ice to the total weight
  • the ice supply device of the above (11) is provided with a cooling device for cooling the water flowing through the water flow path.
  • the ice making system of the present disclosure is The refrigerant circuit for generating the sherbet ice and the ice supply devices (1) to (12) are provided.
  • the sherbet ice generated by the refrigerant circuit is stored in the ice storage tank, and the water flow path through which the water flows joins the supply path for taking out the sherbet ice from the ice storage tank. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user.
  • the refrigerant circuit With a compressor, A first heat exchanger that dissipates heat from the refrigerant compressed by the compressor, It is desirable to include a second heat exchanger that cools the cooled medium by exchanging heat between the refrigerant radiated by the first heat exchanger and the cooled medium that is the raw material of the sherbet ice.
  • sherbet ice can be generated by cooling the cooled medium with the refrigerant flowing through the refrigerant circuit.
  • the refrigerant circuit It is desirable to further include a third heat exchanger that cools the water by exchanging heat between the refrigerant radiated by the first heat exchanger and the water flowing through the water flow path. With such a configuration, it is possible to cool the water flowing through the water flow path by utilizing the refrigerant of the refrigerant circuit that produces sherbet ice.
  • the ice making system of (15) further includes a water tank for storing water cooled by the third heat exchanger. With such a configuration, the cooled water can be stably supplied to the supply path.
  • the ice making system of the above (16) is A third temperature sensor that detects the temperature of the water in the water tank, A control valve that controls the flow of refrigerant in the third heat exchanger, It is desirable to include a second control unit that controls the operation of the control valve based on the detection temperature of the third temperature sensor. With such a configuration, the temperature of the water in the water tank can be appropriately controlled.
  • the third temperature sensor is arranged on the lower side in the water tank. According to this configuration, the third temperature sensor can detect the lower temperature of the water stored in the water tank, and by controlling the operation of the control valve based on this temperature, the inside of the water tank. It is possible to prevent the water from being cooled (frozen) more than necessary.
  • the ice making system of the present disclosure is Ice making equipment and The ice supply device according to any one of (1) to (12) above is provided.
  • a water channel through which water flows joins a supply path for taking out sherbet ice from an ice storage tank. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user.
  • FIG. 1 is an explanatory view of an ice making system S according to the first embodiment of the present disclosure
  • FIG. 2 is an explanatory view of an ice making machine 1 in the ice making system S shown in FIG. 1
  • FIG. 3 is a diagram. It is explanatory drawing of the ice supply apparatus C including the ice storage tank T in the ice making system S shown in 1.
  • the ice making system S includes an ice making device I and an ice supply device C.
  • the ice making device I and the ice storage tank T which is a component of the ice supply device C, are connected by a pipe.
  • the ice making device I produces sherbet ice from the cooled medium by heat exchange with the refrigerant.
  • seawater is used as a medium to be cooled, and the ice making device I generates fine ice from seawater as a raw material, and stores the sherbet ice mixed with seawater, which is a mixture of the generated fine ice and seawater, in an ice storage tank.
  • Sherbet ice is also called slurry ice, ice slurry, slurry ice, sluff ice, or liquid ice.
  • salt water containing salt in water can be used as used herein, "water” includes industrial water, tap water, and fresh water that are substantially free of salt.
  • the ice making device I includes a compressor 2, a heat source side heat exchanger 3 (first heat exchanger), a four-way switching valve 4, in addition to the ice making machine 1 constituting the user side heat exchanger (second heat exchanger). It includes a user-side expansion valve 5, a heat source-side expansion valve 6, an internal heat exchanger 7, and a receiver 8. These devices form a refrigerant circuit 95 by being connected by a refrigerant pipe 96.
  • the ice maker 1 includes an evaporator 13 (second heat exchanger) including an inner tube 11 and an outer tube 12, and an ice scraping unit 14.
  • the ice maker 1 is a horizontal double-tube ice maker in which the axes of the inner tube 11 and the outer tube 12 are arranged horizontally.
  • the liquid refrigerant passes through most of the annular space 24 between the inner pipe 11 and the outer pipe 12.
  • the inner pipe 11 is an element through which seawater, which is a medium to be cooled, passes through, and is made of a metal material such as stainless steel or iron.
  • the inner tube 11 has a cylindrical shape and is arranged inside the outer tube 12. Both ends of the inner pipe 11 are closed. Inside the inner pipe 11, an ice scraping portion 14 is provided which scoops up the ice generated on the inner peripheral surface of the inner pipe 11 and disperses it in the seawater in the inner pipe 11.
  • a seawater pipe 15 for supplying seawater in the ice storage tank T into the inner pipe 11 is connected to one end side in the axial direction of the inner pipe 11. Further, a sherbet pipe 16 for returning seawater from the inner pipe 11 to the ice storage tank T is connected to the other end side of the inner pipe 11 in the axial direction.
  • the outer tube 12 has a cylindrical shape, and is made of a metal material such as stainless steel or iron like the inner tube 11.
  • a plurality of (three in the illustrated example) refrigerant inlet pipes 17 branched on the downstream side of the utilization side expansion valve 5 are connected to the lower part of the outer pipe 12.
  • a refrigerant outlet pipe 18 leading to the internal heat exchanger 7 is connected to the upper part of the outer pipe 12.
  • three refrigerant inlet pipes 17 are provided, but the number of refrigerant inlet pipes 17 may be 2 or less, or 4 or more.
  • the number of refrigerant outlet pipes 18 is 1, but it may be 2 or more.
  • the ice scraping unit 14 includes a rotating shaft 19, a support bar 20, a blade 21, and a motor 22.
  • the other end of the rotating shaft 19 in the axial direction is provided extending outward from the flange 23 provided at the other end of the inner pipe 11 in the axial direction, and is connected to the motor 22 for driving the rotating shaft 19.
  • Support bars 20 are erected on the peripheral surface of the rotating shaft 19 at predetermined intervals, and blades 21 are attached to the tips of the support bars 20.
  • the blade 21 is made of, for example, a strip-shaped member made of synthetic resin, and has a tapered shape on the front side in the rotation direction.
  • the four-way switching valve 4 is held in the state shown by the solid line in FIG.
  • the high-temperature and high-pressure gaseous refrigerant discharged from the compressor 2 flows into the heat source-side heat exchanger 3 that functions as a condenser via the four-way switching valve 4, and heats and exchanges with air by the operation of the blower fan 10 to condense. Liquefaction.
  • the liquefied refrigerant flows into the utilization-side expansion valve 5 via the heat source-side expansion valve 6, the receiver 8, and the internal heat exchanger 7 in the fully open state.
  • the refrigerant is depressurized to a predetermined low pressure by the expansion valve 5 on the utilization side, and is supplied from the refrigerant inlet pipe 17 into the annular space 24 between the inner pipe 11 and the outer pipe 12 constituting the evaporator 13.
  • the refrigerant ejected into the annular space 24 exchanges heat with the seawater supplied into the inner pipe 11 and evaporates. Seawater containing fine ice generated by cooling by evaporation of the refrigerant flows out from the sherbet pipe 16 and returns to the ice storage tank T. The refrigerant evaporated and vaporized by the ice maker 1 is sucked into the compressor 2. At that time, if the refrigerant in a state of containing liquid that cannot be completely evaporated by the ice maker 1 enters the compressor 2, the compressor 2 fails due to a sudden increase in the internal pressure of the compressor cylinder (liquid compression) or a decrease in the viscosity of the refrigerating machine oil. It causes to.
  • the low-pressure refrigerant leaving the ice maker 1 to protect the compressor 2 exchanges heat with the high-pressure refrigerant that has passed through the receiver 8 in the internal heat exchanger 7, is heated, and returns to the compressor 2.
  • the internal heat exchanger 7 is a double-tube type, and the low-pressure refrigerant leaving the ice maker 1 heats between the high-pressure refrigerant while passing through the space between the inner and outer pipes of the internal heat exchanger 7. It is exchanged, heated and returned to the compressor 2.
  • the ice maker 1 cannot be operated. In this case, a defrost operation (heating operation) is performed to melt the ice in the inner pipe 11.
  • the four-way switching valve 4 is held in the state shown by the broken line in FIG.
  • the high-temperature and high-pressure gaseous refrigerant discharged from the compressor 2 flows into the annular space between the inner pipe 11 and the outer pipe 12 of the ice maker 1 via the four-way switching valve 4 and the internal heat exchanger 7, and is inside. It condenses and liquefies by exchanging heat with seawater containing ice in the pipe 11.
  • the liquefied refrigerant flows into the heat source side expansion valve 6 via the utilization side expansion valve 5, the internal heat exchanger 7, and the receiver 8 in the fully open state, is depressurized to a predetermined low pressure by the heat source side expansion valve 6, and serves as an evaporator. It flows into the functioning heat source side heat exchanger 3.
  • the refrigerant flowing into the heat source side heat exchanger 3 that functions as an evaporator exchanges heat with air by the operation of the blower fan 10, vaporizes, and is sucked into the compressor 2.
  • the ice supply device C is a device that supplies the sherbet ice produced by the ice making device I to the user.
  • the ice supply device C includes an ice storage tank T for storing sherbet ice, a supply path 31, and a water flow path 80 through which water flows, which joins the supply path 31.
  • the supply path 31 has an on-off valve. By opening the on-off valve, sherbet ice is supplied to the user.
  • the on-off valve is the solenoid valve 37, but it may be a valve or the like that is manually opened by the user.
  • the ice supply device C includes a control device 25 which is a control unit. As shown in FIG.
  • the control device 25 includes a CPU 25a, a memory 25b such as a RAM and a ROM, and a transmission / reception unit 25c that transmits / receives to / from an external device, a sensor, or the like.
  • the control device 25 realizes various controls related to the operation of the ice making system S, including the operation control of the ice supply device C, by the CPU 25a executing the computer program stored in the memory 25b.
  • the control device 25 controls the drive of the drive units or actuators of the solenoid valves 37, 73, 91, the proportional control valve 83, and the pumps 32, 38, which will be described later.
  • control device 25 receives the detection signals from the temperature sensors 84 and 92 and the water level sensor 33 at the transmitting / receiving unit 25c. Further, the control device 25 is communicably connected to the control unit 27 of the ice making device I, controls the operation of the ice making device I via the control unit 27, and makes ice via the control unit 27. Receives a signal from the sensor of device I or the like.
  • the main control unit of the ice making system S can be attached to the ice making device I side.
  • the ice storage tank T is made of a metal material such as stainless steel or iron.
  • the ice storage tank T has a rectangular tube shape with a rectangular horizontal cross section.
  • the ice storage tank T is a closed container having a lid portion, but in FIGS. 1 and 3, the lid portion is not shown in order to make it easier to understand the structure of the upper part inside the ice storage tank T.
  • a pump 32 for transferring the seawater in the ice storage tank T into the inner pipe 11 of the ice maker 1 by the seawater pipe 15 is arranged.
  • the sherbet ice in the ice storage tank T can be provided with fluidity. ..
  • a water level sensor 33 is provided in the ice storage tank T. Based on the detection signal from the water level sensor 33, seawater is replenished or discharged, which will be described later.
  • the water level sensor 33 can detect a plurality of water levels in the ice storage tank T, for example, 90%, 70%, 45%, 30%, 25% from the bottom of the height of the ice storage tank T. It is arranged so that the position can be detected.
  • As the water level sensor 33 a generally known sensor can be used.
  • a discharge path 90 for discharging seawater in the ice storage tank T is connected near the bottom of the ice storage tank T.
  • the discharge path 90 has a solenoid valve 91.
  • the supply path 31 is a flow path or aisle for supplying the user with sherbet ice generated by the ice making device I and stored in the ice storage tank T.
  • the supply path 31 has a supply port 39 at the downstream end for discharging the sherbet ice taken out from the ice storage tank T.
  • a pipe, a hose, or a combination thereof can be used as the supply path 31, a pipe, a hose, or a combination thereof can be used.
  • a pump 38 is provided in the supply path 31, and by driving the pump 38, sherbet ice in the ice storage tank T can be sucked and taken out to the outside.
  • the float 40 is a member that floats in the ice storage tank T apart from the inner wall 30 of the ice storage tank T.
  • the float 40 in this embodiment is a hollow body and can be made of a synthetic resin such as vinyl chloride resin (PVC).
  • PVC vinyl chloride resin
  • the float 40 has a square shape in a plan view and a substantially rhombus shape in a side view. More specifically, the upper surface 40a of the float 40 has an upwardly inclined surface that inclines from the outer edge toward the center of the float 40 so as to move away from the liquid surface. Similarly, the bottom surface 40b of the float 40 has a downwardly sloping surface that slopes away from the liquid surface from the outer edge toward the center of the float 40.
  • the shape of the float 40 is not particularly limited in the present disclosure, and a float 40 having a circular shape, a triangular shape, or a polygonal shape having a pentagon or more can be used. Further, the upper surface and / or the bottom surface of the float 40 may be a flat surface instead of an inclined surface.
  • the size of the float 40 is not particularly limited in the present disclosure, but when the float 40 having a square inner wall is floated in the ice storage tank T having a rectangular inner wall in a plan view, the length of one side of the ice storage tank T (the shorter one).
  • the length of one side of the square float 40 can be, for example, 0.3 to 0.5 W.
  • the float 40 having a circular plan view is floated in the ice storage tank T having a circular plan view, if the inner diameter of the ice storage tank T is D, the outer diameter of the circular float 40 is, for example, 0.3 to 0.5 D. can do.
  • An opening 41 penetrating in the vertical direction is formed in the center of the float 40 (center in a plan view).
  • the opening 41 has a circular shape in a plan view.
  • the tip 34a of the hose 34 forming a part of the supply path 31 is inserted into the opening 41 and fixed to the float 40.
  • the hose 34 has a bellows portion 34b on the root side of the tip portion 34a.
  • the bellows portion 34b can be expanded and contracted by a predetermined distance along the longitudinal direction or the axial direction of the hose 34.
  • the end portion of the bellows portion 34b opposite to the tip portion 34a is connected to the diameter-expanded portion 35a of the end portion of the pipe 35 constituting the supply path 31.
  • the position of the pipe 35 is fixed by a fixture (not shown).
  • One end of the chain 36 is fixed to each of the four corners of the square float 40.
  • the other end of the chain 36 is locked to the inner wall 30 of the ice storage tank T.
  • the length of each chain 36 is set to a length that allows vertical movement and horizontal movement within a certain range of the float 40.
  • the float 40 can move up and down within a certain range due to the presence of the bellows portion 34b. Further, the float 40 is restricted from moving horizontally beyond a certain range due to the presence of the chain 36.
  • the supply path 31 is configured by the above-mentioned pipe 35, hose 34, and opening 41.
  • the tip (opening edge) of the opening 41 of the float 40 which is the tip of the supply path 31, functions as an outlet 42 for sucking and taking out the sherbet ice stored in the ice storage tank T.
  • the outlet 42 is located on the bottom surface 40b of the float 40. In other words, the outlet 42 is located below the surface of the sherbet ice stored in the tank body.
  • the vertical position of the outlet 42 is not particularly limited in the present disclosure, but for example, the size, shape, weight, etc. of the float 40 may be selected so as to be located about 10 to 40 cm below the liquid level L of the sherbet ice. it can.
  • the bottom surface 40b of the float 40 has a downwardly inclined surface that inclines from the outer edge of the float 40 toward the outlet 42 so as to move away from the liquid surface, the air in the liquid around the outlet 42 can be removed. It can escape upward along the inclined surface. As a result, the suction of air from the outlet 42 at the tip of the supply path 31 can be further suppressed.
  • the ice supply device C has a return path 50 that branches off from the supply path 31 on the downstream side of the pump 38 arranged in the supply path 31 and returns sherbet ice to the ice storage tank T.
  • the return passage 50 is connected to a sherbet pipe 16 that returns seawater containing ice generated by the ice maker 1 to the ice storage tank T.
  • a safety valve 51 is provided in the return passage 50. The safety valve 51 is opened when the pressure in the return passage 50 exceeds a predetermined pressure. Further, the safety valve 51 is used when the pump 38 is driven even though the solenoid valve 37 provided in the supply path 31 has failed and the sherbet ice cannot be supplied from the supply port 39.
  • a solenoid valve that can be opened and closed can be used instead of the safety valve 51.
  • the solenoid valve is controlled by the CPU 25a of the control device 25 so as to be closed when the sherbet ice is supplied to the user by the supply port 39 of the supply path 31, and the supply port of the supply path 31 is closed. From 39, it is controlled to open when the sherbet ice is not supplied.
  • the sherbet ice can be returned to the ice storage tank T by operating the pump 38 and controlling the solenoid valve to open. As a result, it is possible to impart fluidity to the sherbet ice stored in the ice storage tank T and prevent the sherbet ice from freezing.
  • the pump 38 arranged in the supply path 31 functions as a pump for supplying the sherbet ice in the ice storage tank T to the user from the supply port 39, and also stores ice via the reflux path 50 branching from the supply path 31. It can function as a pump for returning the sherbet ice taken out from the tank T to the ice storage tank T.
  • the sherbet ice supply pump and the reflux pump can be shared.
  • the opening / closing control of the solenoid valve capable of opening / closing control described above by the CPU 25a of the control device 25, it is possible to suppress freezing of the sherbet ice in the ice storage tank T. Specifically, by driving the pump 38 constantly or periodically while the ice making device I is operating, the sherbet ice in the ice storage tank T can be constantly or periodically flowed through the return path and circulated. As a result, it is possible to prevent the sherbet ice near the liquid surface from freezing during ice making.
  • the opening and closing of the solenoid valve is controlled by the CPU 25a of the control device 25 so as to be interlocked with the drive of the pump 38.
  • the sherbet ice in the ice storage tank T is prevented from freezing by constantly or periodically flowing the sherbet ice in the ice storage tank T through the reflux path and circulating the ice. You can also do it.
  • the downstream end of the sherbet pipe 16 is branched into four branch pipes 60 as shown in FIG.
  • a discharge pipe 61 is attached to the downstream end of each branch pipe 60.
  • a plurality of (six in the example shown in FIG. 5) discharge ports 62 are formed on the lower surface of the discharge pipe 61.
  • the branch pipe 60 and the discharge pipe 61 are arranged above the liquid level L of the sherbet ice stored in the ice storage tank T.
  • the downstream end of the seawater supply pipe 70 that supplies seawater to the ice storage tank T is connected to the sherbet pipe 16.
  • the seawater sucked from the seawater acquisition port by a pump (not shown) joins the sherbet pipe 16 via the sterilization / filtration device 72 and the solenoid valve 73, and is supplied to the ice storage tank T from the discharge port 62 of the discharge pipe 61 described above. Will be done.
  • the sterilization / filtration device 72 is a device for removing foreign substances contained in seawater and sterilizing bacteria contained in seawater.
  • the seawater can be replenished to the ice storage tank T using the seawater replenishment pipe 70 based on the detection signal of the water level sensor 33 described above.
  • the ice supply device C has a water flow path 80 through which water flows, which joins the supply path 31 for taking out sherbet ice from the ice storage tank T.
  • the water flow path 80 joins the supply path 31 on the upstream side in the flow direction of the sherbet ice with respect to the pump 38 for sucking and taking out the sherbet ice from the ice storage tank T.
  • the number of pumps required for two can be reduced to one.
  • salt water containing salt in water can also be used.
  • an input unit 26 (see FIG. 4) that is communicably connected to the control device 25 is provided.
  • the user can take out a desired amount of sherbet ice having a desired salt concentration from the supply port 39.
  • the water stored in the water tank 81 is sucked by the pump 38 and joins the supply path 31 via the proportional control valve 83 which is a flow rate adjusting valve.
  • a temperature sensor 84 which is a first temperature sensor, is provided on the downstream side of the confluence of the water flow path 80 and the supply path 31 and on the downstream side of the pump 38 to detect the temperature of sherbet ice. Since there is a correlation between the salt concentration of sherbet ice and the temperature, the salt concentration can be calculated from the detected temperature by detecting the temperature of the sherbet ice with the temperature sensor 84. This calculation can be performed by the CPU 25a of the control device 25.
  • the opening and / or opening time of the proportional control valve 83 is adjusted by the CPU 25a of the control device 25 so that the salt concentration becomes the target value, thereby adjusting the desired salt concentration.
  • the opening degree of the proportional control valve 83 is fully opened, the flow rate of sherbet ice flowing through the supply path 31 and the flow rate flowing through the water flow path 80 are configured to be substantially equal to each other.
  • the concentration of sherbet ice taken out from the solenoid valve 37 can be set to about half the concentration of sherbet ice stored in the ice storage tank T.
  • the opening degree of the proportional control valve 83 when the opening degree of the proportional control valve 83 is set to 50%, the ratio of the flow rate of sherbet ice flowing through the supply path 31 to the flow rate flowing through the water flow path 80 is 2: 1.
  • the concentration of sherbet ice taken out from the solenoid valve 37 can be reduced to about two-thirds of the concentration of sherbet ice stored in the ice storage tank T.
  • the time for fully opening the proportional control valve 83 is set to about half the time during which the pump 38 is operated, the concentration of sherbet ice taken out from the electromagnetic valve 37 is stored in the ice storage tank T. It can be about two-thirds of the concentration of sherbet ice.
  • a concentration sensor 84 (first concentration sensor) that detects the salt concentration may be used.
  • the opening degree and / or opening time of the proportional control valve 83 can be adjusted by the control device 25 so that the salt concentration becomes a target value based on the detected salt concentration.
  • a temperature sensor 92 which is a second temperature sensor, is provided in the ice storage tank T to detect the temperature of the sherbet ice in the ice storage tank T. Based on the temperature of seawater before operation and the temperature of sherbet ice after the start of operation detected by the temperature sensor 92, the salt concentration of the sherbet ice can be determined by the CPU 25a of the control device 25. Then, the CPU 25a of the control device 25 adjusts the flow rate of water merging from the water flow path 80 to the supply path 31 by changing the opening degree and / or opening time of the proportional control valve 83 based on the salinity. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user.
  • the concentration sensor 92 which is the second concentration sensor
  • the temperature sensor 92 which is the second temperature sensor
  • the CPU 25a of the control device 25 can obtain the concentration of sherbet ice in the ice storage tank T by the concentration sensor 92.
  • the temperature of the sherbet ice is detected by the temperature sensor 92, and the salt concentration is calculated by the CPU 25a of the control device 25 from the detected temperature. can do. Then, the CPU 25a of the control device 25 prohibits the operation of taking out the sherbet ice in the ice storage tank T when the calculated salt concentration is not within the predetermined range. If the salt concentration of the sherbet ice in the ice storage tank T is too low, the IPF of the sherbet ice is also low, and the use as sherbet ice is insufficient.
  • the concentration sensor 92 which is the second concentration sensor
  • the temperature sensor 92 which is the second temperature sensor
  • the CPU 25a of the control device 25 has a predetermined range of the salt concentration of the sherbet ice detected by the concentration sensor 92. If not, the operation of taking out the sherbet ice in the ice storage tank T is prohibited.
  • the CPU 25a of the control device 25 controls the solenoid valve 91 and the solenoid valve 73 when it is determined that the salt concentration calculated based on the temperature detected by the temperature sensor 92 exceeds a predetermined value. Specifically, the CPU 25a of the control device 25 opens the solenoid valve 91 when the calculated salt concentration exceeds a predetermined value. As a result, the seawater in the ice storage tank T is discharged to the outside via the discharge path 90. Then, when the first predetermined condition is satisfied, the CPU 25a closes the solenoid valve 91, then opens the solenoid valve 73 to supply seawater to the ice storage tank T. Then, when the second predetermined condition is satisfied, the CPU 25a closes the solenoid valve 73.
  • the salt concentration of the seawater in the ice storage tank T can be increased.
  • the value can be lowered below a predetermined value, and as a result, the ice making device I can be continuously operated. Thereby, the ice making efficiency of the ice making system S can be improved.
  • a salinity sensor can also be used as a means for detecting the concentration of seawater in the ice storage tank T.
  • predetermined value is not particularly limited in the present disclosure, but can be, for example, 7%. If the salt concentration of the sherbet ice in the ice storage tank T exceeds 7%, it becomes difficult to make ice in the ice making machine 1, and the ice making efficiency may decrease.
  • the predetermined value can be appropriately set via an input unit of a control device 25 (not shown). The set predetermined value is stored in the memory 25b. Further, the "first predetermined condition" and the "second predetermined condition” can be, for example, when the water level as a dividing line between water and ice drops to a certain position.
  • the CPU 25a of the control device 25 detects that the water level has dropped to the first position by the water level sensor 33.
  • the first position for example, a position 45% from the bottom of the tank height can be selected from the plurality of water levels detected by the water level sensor 33 described above. Since the pump may be damaged if only ice is handled, the pump is configured to stop drainage and start water supply when the water level described above drops to the first position.
  • the CPU 25a of the control device 25 detects that the water level has risen to the second position by the water level sensor 33.
  • the second position for example, 90% of the positions of the plurality of water levels detected by the water level sensor 33 described above can be selected from the bottom of the tank height.
  • the first position and the second position can be appropriately set via an input unit of a control device 25 (not shown).
  • the set first position and second position are stored in the memory 25b.
  • the following control flow is executed.
  • the CPU 25a of the control device 25 detects the salt concentration of the sherbet ice in the ice storage tank T by the temperature sensor 92 arranged in the ice storage tank T (step S1).
  • the CPU 25a of the control device 25 determines whether or not the salt concentration exceeds 7% (step S2), and if it determines that the salt concentration exceeds 7%, proceeds to step S3.
  • the CPU 25a transmits a command to the control unit 27 of the ice making device I to stop the operation of the ice making device I.
  • the CPU 25a opens the solenoid valve 91 provided in the discharge path 90 connected to the ice storage tank T (step S4). As a result, seawater near the bottom surface of the ice storage tank T is discharged.
  • the discharged seawater may contain some sherbet ice.
  • step S5 the CPU 25a determines whether or not the water level detected by the water level sensor 33 has dropped to a water level lower than the first predetermined condition.
  • the CPU 25a determines in step S5 that the water level has dropped to a water level lower than the first predetermined condition
  • the CPU 25a proceeds to step S6 and closes the solenoid valve 91 in step S6.
  • the CPU 25a opens the solenoid valve 73 (step S7).
  • seawater salt concentration of about 3.5%) is supplied into the ice storage tank T.
  • step S8 the CPU 25a determines whether or not the water level detected by the water level sensor 33 has risen to a water level higher than the second predetermined condition.
  • step S8 When the CPU 25a determines in step S8 that the water level has risen to a level higher than the second predetermined condition, the CPU 25a proceeds to step S9 and closes the solenoid valve 73 in step S9. After that, in step S10, the CPU 25a transmits a command to start the operation of the ice making device I to the control unit of the ice making device I. After performing step S10, the process returns to step S1, and the CPU 25a of the control device 25 detects the salt concentration of the sherbet ice in the ice storage tank T by the temperature sensor 92 arranged in the ice storage tank T. By repeating such steps S1 to S10, the ice making device I can be continuously operated.
  • the target salt concentration in the ice storage tank T can be, for example, 3.5 to 7%. By performing such control, the ice making device I can be continuously operated.
  • the CPU 25a of the control device 25 sets the salt concentration of the seawater in the ice storage tank T to the target salt concentration.
  • the solenoid valve 91 of the discharge path 90 and the solenoid valve 73 of the seawater supply pipe 70 may be controlled.
  • the control in this case can be controlled as follows.
  • the CPU 25a of the control device 25 recognizes the salt concentration of the seawater supplied from the seawater supply pipe 70.
  • the CPU 25a of the control device 25 calculates the amount of seawater discharged from the ice storage tank T and the amount of seawater supplied from the seawater supply pipe 70 when the salt concentration of the seawater in the ice storage tank T reaches a predetermined value. Therefore, the electromagnetic valve 91 and the electromagnetic valve 73 can be controlled so that the salt concentration when different concentrations of salt water are mixed in the ice storage tank T becomes the target salt concentration.
  • the first predetermined condition can be the amount of seawater discharged from the ice storage tank T
  • the second predetermined condition can be the amount of seawater supplied from the seawater supply pipe 70.
  • Water is supplied to the water tank 81 via the control valve 86.
  • a float switch 87 is arranged in the water tank 81, and the control valve 86 is controlled to open and close based on the detection signal from the float switch 87, and the water supply to the water tank 81 is started and stopped. ..
  • the water flow path 80 through which water flows joins the supply path 31 for taking out sherbet ice from the ice storage tank T.
  • the salt concentration of the sherbet ice supplied to the user can be easily adjusted by adjusting the flow rate of the water merging into the supply path 31.
  • the flow rate of water from the water flow path 80 to be merged with the supply path 31 is adjusted. Since the salt concentration of the sherbet ice can be adjusted simply by doing so, the usability of the ice supply device C is improved.
  • the pump 38 is arranged on the downstream side in the flow direction of the sherbet ice from the confluence portion where the water flow path 80 merges with the supply path 31.
  • the pump 38 By disposing the pump 38 on the downstream side in the flow direction of the sherbet ice from the confluence portion, the sherbet ice and water can be flowed by one pump.
  • the proportional control valve 83 is provided in the water flow path 80, and proportional control is performed by the CPU 25a of the control device 25 so that the salt concentration of the sherbet ice after merging becomes a target value.
  • the opening and / or opening time of the valve 83 is controlled.
  • the salt concentration of the sherbet ice after merging can be adjusted only by controlling the opening degree and / or opening time of the proportional control valve 83 provided in the water flow path 80.
  • the temperature sensor 84 for detecting the temperature of the sherbet ice is provided on the downstream side in the flow direction of the sherbet ice from the confluence of the supply path 31 and the water flow path 80, and is detected.
  • the CPU 25a of the control device 25 controls the opening and / or opening time of the proportional control valve 83 so that the temperature becomes the target value.
  • the proportional control valve 83 By controlling the proportional control valve 83 using the temperature detected by the temperature sensor 84, the salt concentration of the sherbet ice after merging can be adjusted. In this case, since there is a correlation between the salt concentration of sherbet ice and the temperature, the salt concentration of sherbet ice can be calculated from the temperature detected by the temperature sensor 84.
  • the temperature sensor 92 is arranged in the ice storage tank T, and the temperature of the seawater before the operation and the temperature of the sherbet ice after the start of the operation are detected by the temperature sensor 92. Based on this, the CPU 25a of the control device 25 calculates the salt concentration of the sherbet ice. Then, the salt concentration of the sherbet ice supplied to the user can be adjusted by adjusting the flow rate of the water merging from the water flow path 80 to the supply path 31 based on the calculated salt concentration.
  • the temperature of the sherbet ice is detected by the temperature sensor 92, and the salt concentration is calculated by the CPU 25a of the control device 25 from the detected temperature. Then, the CPU 25a of the control device 25 prohibits the operation of taking out the sherbet ice in the ice storage tank T when the calculated salt concentration is not within the predetermined range. If the salt concentration of the sherbet ice in the ice storage tank T is too low, the IPF of the sherbet ice is also low, and the use as sherbet ice is insufficient. By prohibiting the operation of taking out the sherbet ice in the ice storage tank when the detected salt concentration is not within the predetermined range, it is possible to suppress the supply of the sherbet ice in an insufficient state to the user.
  • control device 25 is provided with an input unit 26 communicatively connected, and the user can input the salt concentration and amount of sherbet ice taken out from the ice storage tank T. , A desired amount of sherbet ice having a desired salt concentration can be taken out from the supply port 39.
  • the supply path 31 has an outlet 42 for taking out the sherbet ice in the ice storage tank T, and this outlet 42 is the liquid level of the sherbet ice in the ice storage tank T. It is arranged below by a predetermined distance from L. Since the fine ice that constitutes sherbet ice has a lower specific density than seawater, it moves upward due to buoyancy. Therefore, the sherbet ice near the liquid surface in the ice storage tank T has a higher IPF than the sherbet ice near the bottom surface. .. High IPF sherbet ice can be supplied to the user by taking out the sherbet ice near the liquid level through the outlet 42 arranged below the liquid level L of the sherbet ice in the ice storage tank T by a predetermined distance.
  • the water flow path 80 through which water flows joins the supply path 31 for taking out sherbet ice from the ice storage tank T.
  • the salt concentration of the sherbet ice supplied to the user can be easily adjusted by adjusting the flow rate of the water merging into the supply path 31.
  • the flow rate of water from the water flow path 80 to be merged with the supply path 31 is adjusted. Since the salt concentration of sherbet ice can be easily adjusted just by doing so, the usability of the ice making system S is improved.
  • FIG. 7 is an explanatory diagram of the ice making system according to the second embodiment of the present disclosure.
  • FIG. 8 is an explanatory diagram of the control device of the ice making system shown in FIG.
  • the ice making system S of the present embodiment includes an ice making device I and an ice supply device C as in the first embodiment. Further, the ice making system S of the present embodiment includes a cooling device 100 and a temperature sensor (third temperature sensor) 103.
  • the cooling device 100 cools the water flowing through the water flow path 80.
  • the third temperature sensor 103 detects the temperature of the water cooled by the cooling device 100.
  • the cooling device 100 and the third temperature sensor 103 of the present embodiment are arranged in the water tank 81 which is a component of the ice supply device C.
  • the cooling device 100 is composed of a heat exchanger (third heat exchanger).
  • the heat exchanger constituting the cooling device 100 is also referred to as a cooling heat exchanger 100.
  • the cooling heat exchanger 100 is inserted into the water tank 81 and exchanges heat with the water in the water tank 81.
  • the cooling heat exchanger 100 can adopt, for example, a configuration in which a heat transfer tube through which a refrigerant flows is wound in a coil shape.
  • the cooling heat exchanger 100 of the present embodiment is supplied with the refrigerant used in the ice making device I.
  • the ice making device I includes an ice making machine 1, a compressor 2, and a heat source side heat exchanger (first heat exchanger) 3 that constitute a user-side heat exchanger (second heat exchanger).
  • a four-way switching valve 4 a utilization-side expansion valve 5, a heat source-side expansion valve 6, an internal heat exchanger 7, and a receiver 8.
  • These devices form a refrigerant circuit 95 by being connected by a refrigerant pipe 96.
  • the branch pipe 97 is branched.
  • Refrigerant pipe 96b between the outflow part 1a of the gas refrigerant in the ice maker 1 and the suction part 2a of the gas refrigerant of the compressor 2, more specifically, the refrigerant pipe between the internal heat exchanger 7 and the four-way switching valve 4.
  • the second branch pipe 98 branches from 96b.
  • the first branch pipe 97 is connected to the refrigerant inlet 100a of the cooling heat exchanger 100.
  • the second branch pipe 98 is connected to the refrigerant outlet 100b of the cooling heat exchanger 100.
  • the refrigerant radiated by the heat source side heat exchanger 3 passes through the heat source side expansion valve 6 and the receiver 8, then branches from the refrigerant pipe 96a to the first branch pipe 97 and flows into the cooling heat exchanger 100.
  • the refrigerant that has passed through the cooling heat exchanger 100 joins the refrigerant pipe 96b through the second branch pipe 98, passes through the four-way switching valve 4, and is sucked into the compressor 2.
  • the cooling heat exchanger 100 is provided in the refrigerant circuit 95 in parallel with the ice maker 1.
  • the first branch pipe 97 is provided with a cooling expansion valve 101 for reducing the pressure of the refrigerant.
  • the liquid refrigerant flowing through the first branch pipe 97 is depressurized by the cooling expansion valve 101 to become a low-temperature low-pressure gas-liquid two-phase refrigerant, which is supplied to the cooling heat exchanger 100.
  • the cooling heat exchanger 100 heat exchange is performed between the water in the water tank 81 and the refrigerant. By this heat exchange, the refrigerant absorbs heat from the water in the water tank 81 and evaporates, and the water in the water tank 81 is cooled.
  • the cooling expansion valve 101 supplies the refrigerant to the cooling heat exchanger 100 by opening, and stops the supply of the refrigerant to the cooling heat exchanger 100 by closing. Therefore, the cooling expansion valve 101 functions as a control valve that controls the flow of the refrigerant to the cooling heat exchanger 100.
  • the cooling expansion valve 101 opens and closes based on the temperature detected by the third temperature sensor 103. Specifically, when the temperature detected by the third temperature sensor 103 exceeds a predetermined upper limit temperature T th1 , the cooling expansion valve 101 opens and the water in the water tank 81 is cooled. When the temperature of the water detected by the third temperature sensor 103 falls below the predetermined lower limit temperature T th2 , the cooling expansion valve 101 closes and the cooling of the water in the water tank 81 stops.
  • the upper limit temperature T th1 can be set to a temperature at which the sherbet ice that has merged with water in the supply path 31 does not excessively melt.
  • the upper limit temperature T th1 can be 5 ° C.
  • the lower limit temperature T th2 can be set to a temperature at which the water in the water tank 81 does not freeze.
  • the lower limit temperature T th2 can be 2 ° C.
  • the third temperature sensor 103 is arranged on the lower side of the water tank 81 (below the center in the vertical direction of the water tank 81). Therefore, the lower temperature of the water in the water tank 81 can be detected.
  • the third temperature sensor 103 is preferably arranged below the cooling heat exchanger 100.
  • the third temperature sensor 103 is more preferably arranged near the bottom surface of the water tank 81.
  • the second branch pipe 98 is provided with a fifth temperature sensor 105.
  • the fifth temperature sensor 105 detects the temperature of the refrigerant after passing through the cooling heat exchanger 100. When the cooling expansion valve 101 is open, the opening degree of the cooling expansion valve 101 is adjusted so that the degree of superheat of the refrigerant obtained using the detection result of the fifth temperature sensor 105 becomes a predetermined set value. To.
  • the opening / closing operation of the cooling expansion valve 101 is controlled by the control unit (second control unit) 27 of the ice making device I.
  • the control unit 27 includes a CPU 27a, a memory 27b such as a RAM and a ROM, and a transmission / reception unit 27c that transmits / receives to / from an external device, a sensor, or the like. ..
  • the control unit 27 realizes various controls related to the operation of the ice making system S, including the operation control of the ice making device I, by the CPU 27a executing the computer program stored in the memory 27b.
  • the control unit 27 controls the drive of the compressor 2, the four-way switching valve 4, the expansion valves 5, 6, 101 and the like.
  • the control unit 27 receives a detection signal from the fifth temperature sensor 105 or the like at the transmission / reception unit 27c.
  • the control unit 27 is communicably connected to the control device 25 of the ice supply device C, and acquires the detection results of the temperature sensors 103, 104, etc. received by the control device 25.
  • a fourth temperature sensor 104 is provided in the water flow path 80.
  • the fourth temperature sensor 104 detects the temperature of water immediately before merging with the supply path 31. If the temperature of the water merging into the supply path 31 is high, the sherbet ice after merging tends to melt, and the salt concentration of the sherbet ice may decrease and the temperature may rise rapidly. Therefore, the temperature of the water before merging is detected by the fourth temperature sensor 104, and the opening degree of the proportional control valve 83 is adjusted based on the detection result. The opening degree of the proportional control valve 83 is adjusted by the control device 25 as in the first embodiment.
  • FIG. 9 is a flowchart showing an example of water temperature control in the water tank.
  • the control unit 27 cools the water in the water tank 81 according to the procedure shown in FIG. 9 and maintains the water temperature within a predetermined range.
  • the control unit 27 acquires the water temperature T by receiving a detection signal from the third temperature sensor 103 in the water tank 81 (step S11).
  • control unit 27 determines whether or not the water temperature T exceeds a predetermined upper limit temperature T th1 (step S12).
  • the upper limit temperature T th1 can be 5 ° C. as described above.
  • the control unit 27 executes control to open the cooling expansion valve 101 to cool the water in the water tank 81 (step S13).
  • step S12 determines whether or not the water temperature T is below the predetermined lower limit temperature T th2 (step S14).
  • the lower limit temperature T th2 can be 2 ° C. as described above.
  • step S15 controls to close the cooling expansion valve 101 (step S15). Specifically, the control unit 27 closes the cooling expansion valve 101 when the cooling expansion valve 101 is open, and maintains the closed state when the cooling expansion valve 101 is closed. As a result, the cooling of the water in the water tank 81 is stopped.
  • step S16 When the judgment in step S14 is negative (NO), the control unit 27 maintains the open / closed state of the cooling expansion valve 101 (step S16). Specifically, the control unit 27 maintains an open state when the cooling expansion valve 101 is open, and maintains a closed state when the cooling expansion valve 101 is closed.
  • control unit 27 can maintain the temperature of the water in the water tank 81 within a predetermined range T th1 to T th2.
  • the control device 25 of the present embodiment adjusts the opening degree of the proportional control valve 83 according to the temperature of the water flowing through the water flow path 80. Specifically, the control device 25 stores ice based on the temperature (salt concentration) of the sherbet ice in the ice storage tank T, the temperature of the sherbet ice (salt concentration) that the user wants to take out, and the temperature of the water to be merged with the sherbet ice. The amount of water to be merged with the sherbet ice in the tank T is obtained, and the opening degree of the proportional control valve 83 is adjusted.
  • the control device 25 determines that the temperature of the water flowing through the water flow path 80 is 2 ° C.
  • the opening degree of the proportional control valve 83 is different between the case where the temperature is 5 ° C. Specifically, the control device 25 makes the opening degree of the proportional control valve 83 smaller when the water temperature is 5 ° C. than when the water temperature is 2 ° C.
  • the opening degree of the proportional control valve 83 is the same when the temperature of the water is 2 ° C. and when the temperature is 5 ° C., the water at 2 ° C. is produced when the water at 5 ° C. is merged.
  • the IPF of sherbet ice changes significantly and reaches the set temperature earlier than when merging. Therefore, there is a high possibility that the temperature of sherbet ice will exceed the set temperature.
  • the control device 25 of the present embodiment reduces the change in IPF by making the opening degree of the proportional control valve 83 smaller when the water temperature is 5 ° C. than when the water temperature is 2 ° C., and the set temperature. It takes longer to reach. As a result, it is possible to prevent the temperature of the sherbet ice from exceeding the set temperature.
  • the control device 25 since the water temperature in the water tank 81 is controlled to 2 ° C. to 5 ° C., the control device 25 sets the lowest 2 ° C. as the "reference temperature” and sets the opening degree of the proportional control valve 83 at this time. Is the "reference opening”. When the water temperature exceeds the reference temperature, the control device 25 operates the opening degree of the proportional control valve 83 in the direction of closing from the reference opening degree. Further, the control device 25 is configured to operate the proportional control valve 93 more in the closing direction as the temperature of the water exceeding the reference temperature becomes higher.
  • FIG. 10 is a flowchart showing an example of control of the proportional control valve.
  • the control device 25 controls the opening degree of the proportional control valve according to the procedure shown in FIG. 10 and adjusts the temperature of the sherbet ice to the set temperature.
  • the control device 25 acquires the water temperature by receiving a detection signal from the fourth temperature sensor 104 provided in the water flow path 80 (step S21).
  • control device 25 calculates the difference between the water temperature and the reference temperature (for example, 2 ° C.) (step S22). Then, the control device 25 calculates the operation amount (close amount) of the proportional control valve 83 from the reference opening degree by using this difference (step S23). Next, the control device 25 operates the proportional control valve 83 according to the calculated operation amount to merge water from the water flow path 80 into the supply path 31 (step S24).
  • the ice supply device C and the ice making system S of the second embodiment have the following effects in addition to the effects of the first embodiment.
  • cooled water flows through the water flow path 80. Therefore, it is possible to suppress the melting of sherbet ice by the merged water and supply the high IPF sherbet ice to the user.
  • the ice supply device C includes a cooling device 100 that cools the water flowing through the water flow path 80. Therefore, it is possible to suppress the melting of sherbet ice by the merged water and supply the user with high IPF sherbet ice.
  • the ice making system S of the second embodiment described above includes a refrigerant circuit 95 for generating sherbet ice and an ice supply device C. Therefore, the sherbet ice generated by the refrigerant circuit 95 can be stored in the ice storage tank T, and water can be merged with the supply path 31 for taking out the sherbet ice from the ice storage tank T. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user.
  • the refrigerant circuit 95 includes a compressor 2, a heat source side heat exchanger (first heat exchanger) 3 that dissipates heat from the refrigerant compressed by the compressor 2, and a heat source side heat exchanger. It includes an ice maker 1 which is a user-side heat exchanger (second heat exchanger) that exchanges heat between the refrigerant radiated in 3 and the cooled medium used as a raw material for sherbet ice to cool the cooled medium. Therefore, the cooling medium can be cooled by the refrigerant flowing through the refrigerant circuit 95 to generate sherbet ice.
  • the refrigerant circuit 95 exchanges heat between the refrigerant dissipated by the heat source side heat exchanger 3 and the water flowing through the water flow path 80 to cool the water (first).
  • 3 Heat exchanger) 100 is further included. Therefore, the water flowing through the water flow path 80 can be cooled by using the refrigerant of the refrigerant circuit 95 that generates sherbet ice.
  • a water tank 81 for storing water cooled by the cooling heat exchanger 100 is further provided. Therefore, the cooled water can be stably supplied to the supply path 31.
  • the third temperature sensor 103 that detects the temperature of the water in the water tank 81
  • the cooling expansion valve (control valve) 101 that controls the flow of the refrigerant in the cooling heat exchanger 100.
  • a control unit (second control unit) 27 that controls the operation of the cooling expansion valve 101 based on the detection temperature of the third temperature sensor 103 is provided. Therefore, the temperature of the water in the water tank 81 can be appropriately controlled.
  • the third temperature sensor 103 is arranged on the lower side in the water tank 81. Therefore, it is possible to detect the lowest possible temperature in the water stored in the water tank 81, and by controlling the operation of the cooling expansion valve 101 based on this temperature, the water in the water tank 81 can be detected. It is possible to suppress cooling (freezing) more than necessary.
  • the ice storage tank has a rectangular tube shape having a rectangular horizontal cross section, but the present disclosure is not limited to this.
  • the ice storage tank may be a tank having a cylindrical shape with a circular horizontal cross section, or a tank having a polygonal shape with a horizontal cross section.
  • a type of evaporator that ejects the refrigerant with a nozzle in the annular space between the inner pipe and the outer pipe can be used.
  • a horizontal double-tube ice maker in which the inner pipe and the outer pipe are arranged so that the axes are horizontal has been exemplified.
  • the present disclosure is not particularly limited to ice makers having various shapes and structures, such as a vertical double-tube ice maker in which the axes of the inner tube and the outer tube are arranged to be vertical. Can be adopted.
  • the adjustment of the salt concentration and the amount of sherbet ice supplied to the user, which is input to the input unit 26, is not exemplified, but for example, the value detected by the first temperature sensor 84 is used.
  • the salt concentration of the sherbet ice can be adjusted by controlling the opening degree of the proportional control valve 83 so that the temperature corresponds to the target salt concentration.
  • a sensor (not shown) capable of measuring the flow rate is provided in the vicinity of the solenoid valve 37, and the sherbet ice is opened by opening the solenoid valve 37 until the target amount of sherbet ice is supplied. Supply amount can be adjusted.
  • the cooling heat exchanger as the cooling device may be arranged outside the water tank.
  • a water circuit that draws water from the water tank by a pump and circulates it can be provided, and a cooling heat exchanger can be provided in this water circuit.
  • the cooling heat exchanger as the cooling device may be provided in a refrigerant circuit different from the refrigerant circuit of the ice making device.
  • the cooling device may not use a refrigerant.
  • the water temperature was detected by the temperature sensor provided in the water flow path for controlling the proportional control valve, but the water temperature may be detected by the temperature sensor in the water tank.
  • the proportional control valve can be controlled more accurately by detecting the water temperature immediately before merging into the supply path by the temperature sensor provided in the water flow path.
  • control of the proportional control valve may be feedback control based on the temperature or salinity of the sherbet ice after merging with water.
  • the temperature sensor may be provided not only on the lower side but also on the upper side in the water tank.
  • the temperature range of water in the water tank 2 ° C. to 5 ° C., is an example, and the temperature range may be different from this.

Abstract

An ice supply device (C) is provided with: an ice storage tank (T) for storing sherbet ice; a supply passage (31) through which the sherbet ice is removed from the ice storage tank (T); and a water flow passage (80) that converges with the supply passage (31) and through which water flows.

Description

氷供給装置及び製氷システムIce supply device and ice making system
 本開示は氷供給装置及び製氷システムに関する。 This disclosure relates to an ice supply device and an ice making system.
 海水魚等を冷蔵するために海水等の塩水から生成されるシャーベット氷を用いる場合がある。製氷装置で生成されたシャーベット氷は貯氷タンクに貯留され、随時、ポンプによりユーザに供給される。 Sherbet ice produced from saltwater such as seawater may be used to refrigerate saltwater fish. The sherbet ice produced by the ice maker is stored in an ice storage tank and pumped to the user at any time.
 シャーベット氷を用いて海水魚を冷蔵する場合、魚種や大きさによって、保冷に適した温度が異なることが知られている。保冷対象の海水魚に適した温度未満の低温で当該海水魚を保冷すると、海水魚の魚体が凍結して、その商品価値が大きく損なわれる恐れがある。 When saltwater fish are refrigerated using sherbet ice, it is known that the temperature suitable for refrigeration differs depending on the fish species and size. If the saltwater fish is kept cold at a temperature lower than the temperature suitable for the saltwater fish to be kept cold, the body of the saltwater fish may freeze and its commercial value may be significantly impaired.
 そこで、製氷装置で生成されたシャーベット氷を使用箇所に供給するに際し、当該シャーベット氷の塩分濃度を調製することが提案されている(例えば、特許文献1参照)。なお、シャーベット氷の温度と塩分濃度との間には相関関係が存在しており、塩分濃度を調整することで間接的に温度を調整することができる。 Therefore, it has been proposed to adjust the salt concentration of the sherbet ice when supplying the sherbet ice produced by the ice making device to the place of use (see, for example, Patent Document 1). There is a correlation between the temperature of sherbet ice and the salinity, and the temperature can be indirectly adjusted by adjusting the salinity.
 特許文献1記載の塩水混合シャーベット状アイスの製造装置では、貯氷タンクに真水を注水することで当該貯氷タンク内の塩水混合シャーベット状アイスの塩分濃度を調整し、調整後のシャーベット状のアイスを貯氷タンクから取り出している。 In the salt water mixed sherbet-shaped ice manufacturing apparatus described in Patent Document 1, the salt concentration of the salt water mixed sherbet-shaped ice in the ice storage tank is adjusted by injecting fresh water into the ice storage tank, and the adjusted sherbet-shaped ice is stored. I'm taking it out of the tank.
特開2008-281293号公報Japanese Unexamined Patent Publication No. 2008-281293
 しかし、特許文献1記載の製造装置では、生成後のシャーベット氷が貯留されている貯氷タンクに真水を注水することで当該シャーベット氷の塩分濃度を調整しているので、或る特定の塩分濃度を有するシャーベット氷しか得ることができない。このため、種類が異なる海水魚を冷蔵したい場合、シャーベット氷を当該海水魚に適した塩分濃度に調整することが難しい。 However, in the manufacturing apparatus described in Patent Document 1, the salt concentration of the sherbet ice is adjusted by injecting fresh water into the ice storage tank in which the produced sherbet ice is stored, so that a specific salt concentration can be adjusted. Only sherbet ice can be obtained. Therefore, when it is desired to refrigerate different types of saltwater fish, it is difficult to adjust the sherbet ice to a salt concentration suitable for the saltwater fish.
 本開示は、ユーザに供給されるシャーベット氷の塩分濃度を調整することができる氷供給装置及び製氷システムを提供することを目的としている。 It is an object of the present disclosure to provide an ice supply device and an ice making system capable of adjusting the salt concentration of sherbet ice supplied to a user.
(1)本開示の氷供給装置は、
 シャーベット氷を貯留する貯氷タンクと、前記貯氷タンクからシャーベット氷を取り出す供給路と、前記供給路に合流する、水が流れる水流路と、を備えている。
(1) The ice supply device of the present disclosure is
It is provided with an ice storage tank for storing sherbet ice, a supply path for taking out sherbet ice from the ice storage tank, and a water channel through which water flows, which joins the supply path.
 本開示の氷供給装置では、貯氷タンクからシャーベット氷を取り出す供給路に、水が流れる水流路が合流している。これにより、ユーザに供給されるシャーベット氷の塩分濃度を調整することができる。 In the ice supply device of the present disclosure, a water channel through which water flows joins a supply path for taking out sherbet ice from an ice storage tank. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user.
(2)前記(1)の氷供給装置において、前記水流路が前記供給路に合流する合流部よりも、シャーベット氷の流れ方向下流側に配設されるポンプを更に備えていることが望ましい。合流部よりも、シャーベット氷の流れ方向下流側にポンプを配設することで、1台のポンプでシャーベット氷と水を流動させることができる。 (2) It is desirable that the ice supply device of the above (1) further includes a pump arranged on the downstream side in the flow direction of sherbet ice from the confluence portion where the water flow path joins the supply path. By arranging the pump on the downstream side in the flow direction of the sherbet ice from the confluence portion, the sherbet ice and water can be flowed by one pump.
(3)前記(1)又は(2)の氷供給装置において、前記水流路に設けられた流量調整弁と、合流後のシャーベット氷の塩分濃度が目標値となるように前流量調整弁を制御する制御部とを更に備えていることが望ましい。水流路に設けられた流量調整弁を制御部で制御することにより合流後のシャーベット氷の塩分濃度を調整することができる。 (3) In the ice supply device of (1) or (2), the flow rate adjusting valve provided in the water flow path and the front flow rate adjusting valve are controlled so that the salt concentration of sherbet ice after merging becomes a target value. It is desirable that the control unit is further provided. By controlling the flow rate adjusting valve provided in the water flow path by the control unit, the salt concentration of the sherbet ice after merging can be adjusted.
(4)前記(3)の氷供給装置において、前記合流部よりもシャーベット氷の流れ方向下流側に、シャーベット氷の温度を検出する第1温度センサ又は当該シャーベット氷の塩分濃度を検出する第1濃度センサを更に備え、
 前記制御部は、前記第1温度センサにより検出された温度又は前記第1濃度センサにより検出された濃度が目標値になるように前記流量調整弁を制御することが望ましい。第1温度センサ又は第1濃度センサで検出された温度又は濃度を用いて流量調整弁を制御することで合流後のシャーベット氷の塩分濃度を調整することができる。
(4) In the ice supply device of the above (3), a first temperature sensor for detecting the temperature of the sherbet ice or a first for detecting the salt concentration of the sherbet ice is located downstream of the confluence in the flow direction of the sherbet ice. Equipped with a density sensor
It is desirable that the control unit controls the flow rate adjusting valve so that the temperature detected by the first temperature sensor or the concentration detected by the first concentration sensor becomes a target value. By controlling the flow rate adjusting valve using the temperature or concentration detected by the first temperature sensor or the first concentration sensor, the salt concentration of the sherbet ice after merging can be adjusted.
(5)前記(3)の氷供給装置において、前記合流部よりもシャーベット氷の流れ方向下流側に、シャーベット氷の温度を検出する第1温度センサを更に備え、
 前記制御部は、前記第1温度センサにより検出された温度から塩分濃度を演算し、演算された前記塩分濃度が目標値となるように前記流量調整弁を制御することが望ましい。シャーベット氷の塩分濃度と温度の間には相関関係が存在するので、第1温度センサによりシャーベット氷の温度を検出することで、当該検出した温度から塩分濃度を演算することができる。そして、制御部が、演算された塩分濃度が目標値となるように流量調整弁を制御して供給路に合流する水の流量を調整することで、合流後のシャーベット氷の塩分濃度を調整することができる。
(5) In the ice supply device of the above (3), a first temperature sensor for detecting the temperature of the sherbet ice is further provided on the downstream side in the flow direction of the sherbet ice from the confluence portion.
It is desirable that the control unit calculates the salt concentration from the temperature detected by the first temperature sensor and controls the flow rate adjusting valve so that the calculated salt concentration becomes a target value. Since there is a correlation between the salt concentration of sherbet ice and the temperature, the salt concentration can be calculated from the detected temperature by detecting the temperature of the sherbet ice with the first temperature sensor. Then, the control unit adjusts the salt concentration of the sherbet ice after merging by controlling the flow rate adjusting valve so that the calculated salt concentration becomes the target value and adjusting the flow rate of the water merging into the supply path. be able to.
(6)前記(3)~(5)の氷供給装置において、前記制御部は、前記流量調整弁の開度及び/又は開時間を制御することが望ましい。制御部は、流量調整弁の開度及び/又は開時間を制御することで、供給路に合流する水の流量を調製することができる。 (6) In the ice supply devices (3) to (5), it is desirable that the control unit controls the opening and / or opening time of the flow rate adjusting valve. The control unit can adjust the flow rate of the water merging into the supply path by controlling the opening and / or opening time of the flow rate adjusting valve.
(7)前記(3)~(6)の氷供給装置において、前記貯氷タンク内のシャーベット氷の塩分濃度を検出する第2濃度センサを更に備え、
 前記制御部は、前記第2濃度センサにより検出された塩分濃度が所定範囲内でない場合、前記貯氷タンク内のシャーベット氷の取出操作を禁止することが望ましい。検出された塩分濃度が所定範囲内でない場合に、貯氷タンク内のシャーベット氷の取出操作を禁止することで、ユーザに不十分な状態のシャーベット氷が供給されるのを抑制することができる。
(7) In the ice supply devices (3) to (6), a second concentration sensor for detecting the salt concentration of sherbet ice in the ice storage tank is further provided.
It is desirable that the control unit prohibits the operation of taking out the sherbet ice in the ice storage tank when the salt concentration detected by the second concentration sensor is not within the predetermined range. By prohibiting the operation of taking out the sherbet ice in the ice storage tank when the detected salt concentration is not within the predetermined range, it is possible to suppress the supply of the sherbet ice in an insufficient state to the user.
(8)前記(1)~(7)の氷供給装置において、前記貯氷タンク内のシャーベット氷の温度を検出する第2温度センサと、
 製氷装置の運転前に前記貯氷タンクに供給され前記第2温度センサにより検出された被冷却媒体の温度と、製氷装置の運転開始後に前記貯氷タンク内に貯留され前記第2温度センサにより検出されたシャーベット氷の温度とに基づいて当該シャーベット氷の塩分濃度を演算する塩分濃度演算部とを更に備えていることが望ましい。第2センサにより検出される運転前の被冷却媒体の温度及び運転開始後のシャーベット氷の温度に基づいて、塩分濃度演算部によって当該シャーベット氷の塩分濃度を演算することができる。
(8) In the ice supply devices (1) to (7), the second temperature sensor for detecting the temperature of the sherbet ice in the ice storage tank and the second temperature sensor.
The temperature of the medium to be cooled, which was supplied to the ice storage tank before the operation of the ice making device and detected by the second temperature sensor, and stored in the ice storage tank after the operation of the ice making device was started and detected by the second temperature sensor. It is desirable to further include a salt concentration calculation unit that calculates the salt concentration of the sherbet ice based on the temperature of the sherbet ice. The salinity calculation unit can calculate the salinity of the sherbet ice based on the temperature of the medium to be cooled before the operation and the temperature of the sherbet ice after the start of the operation detected by the second sensor.
(9)前記(1)~(8)の氷供給装置において、貯氷タンクから取り出すシャーベット氷の塩分濃度及び量を受け付ける入力部を更に備えることが望ましい。ユーザは、入力部でシャーベット氷の塩分濃度及び量を入力することによって、所望の塩分濃度を有するシャーベット氷を所望の量だけ取り出すことができる。 (9) In the ice supply devices (1) to (8), it is desirable to further include an input unit for receiving the salt concentration and amount of sherbet ice taken out from the ice storage tank. By inputting the salt concentration and amount of sherbet ice in the input unit, the user can take out a desired amount of sherbet ice having a desired salt concentration.
(10)前記(1)~(9)の氷供給装置において、前記供給路は、前記貯氷タンク内に配設され、当該貯氷タンク内のシャーベット氷を取り出す取出口を有し、
 前記取出口は、前記貯氷タンク内のシャーベット氷の液面から所定距離だけ下方に配置されていることが望ましい。貯氷タンク内のシャーベット氷の液面から所定距離だけ下方に配置されている取出口により液面付近のシャーベット氷を取り出すことで、高IPF(Ice Packing Factor:全体の重量に対する氷の重量の割合(氷重量/(氷重量+水重量))を示す)のシャーベット氷をユーザに供給することができる。
(10) In the ice supply devices (1) to (9), the supply path is arranged in the ice storage tank and has an outlet for taking out sherbet ice in the ice storage tank.
It is desirable that the outlet is arranged below the liquid level of sherbet ice in the ice storage tank by a predetermined distance. High IPF (Ice Packing Factor: ratio of the weight of ice to the total weight) by taking out the sherbet ice near the liquid level by the outlet located below the liquid level of the sherbet ice in the ice storage tank by a predetermined distance. (Ice weight / (ice weight + water weight))) sherbet ice can be supplied to the user.
(11)前記(1)~(10)の氷供給装置において、前記水流路には、冷却された水が流れることが望ましい。冷却された水を供給路に合流させることで、シャーベット氷が溶けるのを抑制し、高IPFのシャーベット氷をユーザに供給することができる。 (11) In the ice supply devices (1) to (10), it is desirable that cooled water flows through the water flow path. By merging the cooled water into the supply path, the sherbet ice can be suppressed from melting and the high IPF sherbet ice can be supplied to the user.
(12)前記(11)の氷供給装置において、前記水流路に流される水を冷却する冷却装置を備えることが望ましい。 (12) It is desirable that the ice supply device of the above (11) is provided with a cooling device for cooling the water flowing through the water flow path.
(13) 本開示の製氷システムは、
 前記シャーベット氷を生成する冷媒回路と、前記(1)~(12)の氷供給装置とを備える。
(13) The ice making system of the present disclosure is
The refrigerant circuit for generating the sherbet ice and the ice supply devices (1) to (12) are provided.
 本開示の製氷システムでは、冷媒回路で生成したシャーベット氷を貯氷タンクに貯留し、貯氷タンクからシャーベット氷を取り出す供給路に、水が流れる水流路が合流している。これにより、ユーザに供給されるシャーベット氷の塩分濃度を調整することができる。 In the ice making system of the present disclosure, the sherbet ice generated by the refrigerant circuit is stored in the ice storage tank, and the water flow path through which the water flows joins the supply path for taking out the sherbet ice from the ice storage tank. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user.
(14)前記(13)の製氷システムにおいて、
 前記冷媒回路が、
  圧縮機と、
  前記圧縮機で圧縮された冷媒を放熱する第1熱交換器と、
  前記第1熱交換器で放熱された冷媒と前記シャーベット氷の原料となる被冷却媒体とを熱交換し当該被冷却媒体を冷却する第2熱交換器と、を含むことが望ましい。
(14) In the ice making system of (13) above,
The refrigerant circuit
With a compressor,
A first heat exchanger that dissipates heat from the refrigerant compressed by the compressor,
It is desirable to include a second heat exchanger that cools the cooled medium by exchanging heat between the refrigerant radiated by the first heat exchanger and the cooled medium that is the raw material of the sherbet ice.
 このような構成によって、冷媒回路を流れる冷媒により被冷却媒体を冷却してシャーベット氷を生成することができる。 With such a configuration, sherbet ice can be generated by cooling the cooled medium with the refrigerant flowing through the refrigerant circuit.
(15)前記(14)の製氷システムにおいて、
 前記冷媒回路が、
  前記第1熱交換器で放熱された冷媒と前記水流路に流される水とを熱交換し当該水を冷却する第3熱交換器をさらに含むことが望ましい。
 このような構成によって、シャーベット氷を生成する冷媒回路の冷媒を利用して水流路に流される水を冷却することができる。
(15) In the ice making system of (14) above,
The refrigerant circuit
It is desirable to further include a third heat exchanger that cools the water by exchanging heat between the refrigerant radiated by the first heat exchanger and the water flowing through the water flow path.
With such a configuration, it is possible to cool the water flowing through the water flow path by utilizing the refrigerant of the refrigerant circuit that produces sherbet ice.
(16)前記(15)の製氷システムは、前記第3熱交換器によって冷却される水を貯留する水タンクをさらに備えることが望ましい。
 このような構成によって、冷却された水を供給路に安定して供給することができる。
(16) It is desirable that the ice making system of (15) further includes a water tank for storing water cooled by the third heat exchanger.
With such a configuration, the cooled water can be stably supplied to the supply path.
(17)前記(16)の製氷システムは、
 前記水タンク内の水の温度を検出する第3温度センサと、
 前記第3熱交換器における冷媒の流れを制御する制御弁と、
 前記第3温度センサの検出温度に基づいて、前記制御弁の動作を制御する第2制御部と、を備えることが望ましい。
 このような構成によって、水タンク内の水の温度を適切に制御することができる。
(17) The ice making system of the above (16) is
A third temperature sensor that detects the temperature of the water in the water tank,
A control valve that controls the flow of refrigerant in the third heat exchanger,
It is desirable to include a second control unit that controls the operation of the control valve based on the detection temperature of the third temperature sensor.
With such a configuration, the temperature of the water in the water tank can be appropriately controlled.
(18)前記(17)の製氷システムにおいて、前記第3温度センサが、前記水タンク内の下部側に配置されることが望ましい。
 この構成によれば、第3温度センサによって、水タンク内に貯留された水の、より低い温度を検出することができ、この温度に基づいて制御弁の動作を制御することで、水タンク内の水が必要以上に冷却される(凍る)のを抑制することができる。
(18) In the ice making system of (17), it is desirable that the third temperature sensor is arranged on the lower side in the water tank.
According to this configuration, the third temperature sensor can detect the lower temperature of the water stored in the water tank, and by controlling the operation of the control valve based on this temperature, the inside of the water tank. It is possible to prevent the water from being cooled (frozen) more than necessary.
(19) 本開示の製氷システムは、
 製氷装置と、
 前記(1)~(12)のいずれかの氷供給装置と
 を備えている。
(19) The ice making system of the present disclosure is
Ice making equipment and
The ice supply device according to any one of (1) to (12) above is provided.
 本開示の製氷システムでは、貯氷タンクからシャーベット氷を取り出す供給路に、水が流れる水流路が合流している。これにより、ユーザに供給されるシャーベット氷の塩分濃度を調整することができる。 In the ice making system of the present disclosure, a water channel through which water flows joins a supply path for taking out sherbet ice from an ice storage tank. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user.
本開示の第1の実施形態に係る製氷システムの説明図である。It is explanatory drawing of the ice making system which concerns on 1st Embodiment of this disclosure. 図1に示される製氷システムにおける製氷機の説明図である。It is explanatory drawing of the ice making machine in the ice making system shown in FIG. 図1に示される製氷システムにおける貯氷タンクを含む氷供給装置の説明図である。It is explanatory drawing of the ice supply apparatus including the ice storage tank in the ice making system shown in FIG. 図3に示される氷供給装置の制御装置の説明図である。It is explanatory drawing of the control device of the ice supply device shown in FIG. 貯氷タンク内の平面説明図である。It is a plane explanatory view in the ice storage tank. 貯氷タンク内の海水の塩分濃度を調整する制御の一例のフローチャートである。It is a flowchart of an example of control which adjusts the salt concentration of seawater in an ice storage tank. 本開示の第2の実施形態に係る製氷システムの説明図である。It is explanatory drawing of the ice making system which concerns on 2nd Embodiment of this disclosure. 図7に示される製氷システムの制御装置の説明図である。It is explanatory drawing of the control device of the ice making system shown in FIG. 水タンク内の水温制御の一例を示すフローチャートである。It is a flowchart which shows an example of the water temperature control in a water tank. 比例制御弁の制御の一例を示すフローチャートである。It is a flowchart which shows an example of the control of a proportional control valve.
 以下、添付図面を参照しつつ、本開示の氷供給装置及び製氷システムを詳細に説明する。なお、本開示はこれらの例示に限定されるものではなく、特許請求の範囲によって示され、特許請求の範囲と均等の意味及び範囲内でのすべての変更が含まれることが意図される。 Hereinafter, the ice supply device and the ice making system of the present disclosure will be described in detail with reference to the attached drawings. It should be noted that the present disclosure is not limited to these examples, and is indicated by the scope of claims, and is intended to include all modifications within the meaning and scope equivalent to the scope of claims.
[第1の実施形態]
 図1は、本開示の第1の実施形態に係る製氷システムSの説明図であり、図2は、図1に示される製氷システムSにおける製氷機1の説明図であり、図3は、図1に示される製氷システムSにおける貯氷タンクTを含む氷供給装置Cの説明図である。
 製氷システムSは、製氷装置Iと、氷供給装置Cとを備えている。製氷装置Iと、氷供給装置Cの構成要素である貯氷タンクTとは配管により接続されている。
[First Embodiment]
FIG. 1 is an explanatory view of an ice making system S according to the first embodiment of the present disclosure, FIG. 2 is an explanatory view of an ice making machine 1 in the ice making system S shown in FIG. 1, and FIG. 3 is a diagram. It is explanatory drawing of the ice supply apparatus C including the ice storage tank T in the ice making system S shown in 1.
The ice making system S includes an ice making device I and an ice supply device C. The ice making device I and the ice storage tank T, which is a component of the ice supply device C, are connected by a pipe.
 [製氷装置I]
 製氷装置Iは、冷媒との熱交換により被冷却媒体からシャーベット氷を生成する。本実施形態では、被冷却媒体として海水が用いられており、製氷装置Iは、海水を原料として微細な氷を生成し、生成した微細な氷と海水が混合した海水混合のシャーベット氷を貯氷タンクTに戻す。シャーベット氷は、スラリー氷、アイススラリー、スラリーアイス、スラッフアイス、リキッドアイスとも呼ばれる。なお、被冷却媒体としては、海水以外に、例えば水に塩分を含有させた塩水を用いることもできる。本明細書における「水」には、実質的に塩分を含まない工業用水、水道水、真水が含まれる。
[Ice maker I]
The ice making device I produces sherbet ice from the cooled medium by heat exchange with the refrigerant. In the present embodiment, seawater is used as a medium to be cooled, and the ice making device I generates fine ice from seawater as a raw material, and stores the sherbet ice mixed with seawater, which is a mixture of the generated fine ice and seawater, in an ice storage tank. Return to T. Sherbet ice is also called slurry ice, ice slurry, slurry ice, sluff ice, or liquid ice. As the cooling medium, in addition to seawater, for example, salt water containing salt in water can be used. As used herein, "water" includes industrial water, tap water, and fresh water that are substantially free of salt.
 製氷装置Iは、利用側熱交換器(第2熱交換器)を構成する製氷機1以外に、圧縮機2、熱源側熱交換器3(第1熱交換器)、四路切換弁4、利用側膨張弁5、熱源側膨張弁6、内部熱交換器7、及びレシーバ8を備えている。これらの機器は、冷媒配管96で接続されることによって冷媒回路95を構成している。 The ice making device I includes a compressor 2, a heat source side heat exchanger 3 (first heat exchanger), a four-way switching valve 4, in addition to the ice making machine 1 constituting the user side heat exchanger (second heat exchanger). It includes a user-side expansion valve 5, a heat source-side expansion valve 6, an internal heat exchanger 7, and a receiver 8. These devices form a refrigerant circuit 95 by being connected by a refrigerant pipe 96.
 製氷機1は、図1~2に示されるように、内管11と外管12とからなる蒸発器13(第2熱交換器)と、氷掻き取り部14とを備えている。製氷機1は、内管11及び外管12の各軸が水平になるように配置された横置き型の二重管式製製氷機である。蒸発器13は、内管11と外管12との間の環状スペース24の大部分を液冷媒が通過する。 As shown in FIGS. 1 and 2, the ice maker 1 includes an evaporator 13 (second heat exchanger) including an inner tube 11 and an outer tube 12, and an ice scraping unit 14. The ice maker 1 is a horizontal double-tube ice maker in which the axes of the inner tube 11 and the outer tube 12 are arranged horizontally. In the evaporator 13, the liquid refrigerant passes through most of the annular space 24 between the inner pipe 11 and the outer pipe 12.
 内管11は、内部を被冷却媒体である海水が通過する要素であり、ステンレスや鉄等の金属材料で作製されている。内管11は円筒形状を呈しており、外管12内に配設される。内管11の両端は閉止されている。内管11の内部には、当該内管11の内周面に生成された氷を掻き上げて内管11内の海水中に分散させる氷掻き取り部14が配設されている。内管11の軸方向一端側に貯氷タンクT内の海水を当該内管11内に供給する海水配管15が接続されている。また、内管11の軸方向他端側に内管11からの海水を貯氷タンクTに戻すシャーベット配管16が接続されている。 The inner pipe 11 is an element through which seawater, which is a medium to be cooled, passes through, and is made of a metal material such as stainless steel or iron. The inner tube 11 has a cylindrical shape and is arranged inside the outer tube 12. Both ends of the inner pipe 11 are closed. Inside the inner pipe 11, an ice scraping portion 14 is provided which scoops up the ice generated on the inner peripheral surface of the inner pipe 11 and disperses it in the seawater in the inner pipe 11. A seawater pipe 15 for supplying seawater in the ice storage tank T into the inner pipe 11 is connected to one end side in the axial direction of the inner pipe 11. Further, a sherbet pipe 16 for returning seawater from the inner pipe 11 to the ice storage tank T is connected to the other end side of the inner pipe 11 in the axial direction.
 外管12は円筒形状を呈しており、内管11と同様にステンレスや鉄等の金属材料で作製されている。外管12の下部には、利用側膨張弁5の下流側で分岐した複数(図示例では3つ)の冷媒入口管17が接続されている。また、外管12の上部には内部熱交換器7に至る冷媒出口管18が接続されている。本実施形態では、3つの冷媒入口管17が設けられているが、冷媒入口管17の数は2以下でもよいし、4以上であってもよい。また、冷媒出口管18の数は1であるが、2以上であってもよい。 The outer tube 12 has a cylindrical shape, and is made of a metal material such as stainless steel or iron like the inner tube 11. A plurality of (three in the illustrated example) refrigerant inlet pipes 17 branched on the downstream side of the utilization side expansion valve 5 are connected to the lower part of the outer pipe 12. Further, a refrigerant outlet pipe 18 leading to the internal heat exchanger 7 is connected to the upper part of the outer pipe 12. In the present embodiment, three refrigerant inlet pipes 17 are provided, but the number of refrigerant inlet pipes 17 may be 2 or less, or 4 or more. The number of refrigerant outlet pipes 18 is 1, but it may be 2 or more.
 氷掻き取り部14は、回転軸19と、支持バー20と、ブレード21と、モータ22とを備えている。回転軸19の軸方向の他端は内管11の軸方向他端に設けられたフランジ23から外部に延びて設けられ、回転軸19を駆動させるモータ22に接続されている。回転軸19の周面には所定間隔で支持バー20が立設されており、この支持バー20の先端にブレード21が取り付けられている。ブレード21は、例えば合成樹脂で作製された帯状の部材からなり、回転方向の前方側は先細形状とされている。 The ice scraping unit 14 includes a rotating shaft 19, a support bar 20, a blade 21, and a motor 22. The other end of the rotating shaft 19 in the axial direction is provided extending outward from the flange 23 provided at the other end of the inner pipe 11 in the axial direction, and is connected to the motor 22 for driving the rotating shaft 19. Support bars 20 are erected on the peripheral surface of the rotating shaft 19 at predetermined intervals, and blades 21 are attached to the tips of the support bars 20. The blade 21 is made of, for example, a strip-shaped member made of synthetic resin, and has a tapered shape on the front side in the rotation direction.
 通常の製氷運転時には、四路切換弁4が、図1において実線で示される状態に保持される。圧縮機2から吐出された高温高圧のガス状冷媒は四路切換弁4を経て凝縮器として機能する熱源側熱交換器3に流入し、送風ファン10の作動により空気と熱交換して凝縮・液化する。液化した冷媒は、全開状態の熱源側膨張弁6、レシーバ8及び内部熱交換器7を経て利用側膨張弁5に流入する。冷媒は、利用側膨張弁5により所定の低圧に減圧され、冷媒入口管17から蒸発器13を構成する内管11と外管12との間の環状スペース24内に供給される。 During normal ice making operation, the four-way switching valve 4 is held in the state shown by the solid line in FIG. The high-temperature and high-pressure gaseous refrigerant discharged from the compressor 2 flows into the heat source-side heat exchanger 3 that functions as a condenser via the four-way switching valve 4, and heats and exchanges with air by the operation of the blower fan 10 to condense. Liquefaction. The liquefied refrigerant flows into the utilization-side expansion valve 5 via the heat source-side expansion valve 6, the receiver 8, and the internal heat exchanger 7 in the fully open state. The refrigerant is depressurized to a predetermined low pressure by the expansion valve 5 on the utilization side, and is supplied from the refrigerant inlet pipe 17 into the annular space 24 between the inner pipe 11 and the outer pipe 12 constituting the evaporator 13.
 環状スペース24内に噴出された冷媒は、内管11内に供給された海水と熱交換して蒸発する。冷媒の蒸発による冷却で生成された微細な氷を含む海水は、シャーベット配管16から流出して貯氷タンクTに戻る。製氷機1で蒸発して気化した冷媒は圧縮機2に吸い込まれる。その際、製氷機1で蒸発しきれずに液体を含んだ状態の冷媒が圧縮機2に入ると、急激な圧縮機シリンダー内部圧力上昇(液圧縮)や冷凍機油の粘度低下により圧縮機2が故障する原因となる。そこで、圧縮機2を保護するために製氷機1を出た低圧冷媒は、レシーバ8を通過した高圧冷媒と、内部熱交換器7において熱交換し、加熱されて圧縮機2に戻る。内部熱交換器7は二重管式であり、製氷機1を出た低圧冷媒は、内部熱交換器7の内管と外管との間のスペースを通る間に高圧冷媒との間で熱交換され、加熱されて、圧縮機2に戻る。 The refrigerant ejected into the annular space 24 exchanges heat with the seawater supplied into the inner pipe 11 and evaporates. Seawater containing fine ice generated by cooling by evaporation of the refrigerant flows out from the sherbet pipe 16 and returns to the ice storage tank T. The refrigerant evaporated and vaporized by the ice maker 1 is sucked into the compressor 2. At that time, if the refrigerant in a state of containing liquid that cannot be completely evaporated by the ice maker 1 enters the compressor 2, the compressor 2 fails due to a sudden increase in the internal pressure of the compressor cylinder (liquid compression) or a decrease in the viscosity of the refrigerating machine oil. It causes to. Therefore, the low-pressure refrigerant leaving the ice maker 1 to protect the compressor 2 exchanges heat with the high-pressure refrigerant that has passed through the receiver 8 in the internal heat exchanger 7, is heated, and returns to the compressor 2. The internal heat exchanger 7 is a double-tube type, and the low-pressure refrigerant leaving the ice maker 1 heats between the high-pressure refrigerant while passing through the space between the inner and outer pipes of the internal heat exchanger 7. It is exchanged, heated and returned to the compressor 2.
 また、製氷機1の内管11内の海水の流れが滞り、内管11内に氷が蓄積される(アイスアキュームレーション)と、当該製氷機1の運転ができなくなる。この場合、内管11内の氷を溶かすためにデフロスト運転(暖房運転)が行われる。このとき、四路切換弁4は、図1において破線で示される状態に保持される。圧縮機2から吐出された高温高圧のガス状冷媒は四路切換弁4及び内部熱交換器7を経て製氷機1の内管11と外管12との間の環状スペース内に流入し、内管11内の氷を含む海水と熱交換して凝縮・液化する。液化した冷媒は、全開状態の利用側膨張弁5、内部熱交換器7及びレシーバ8を経て熱源側膨張弁6に流入し、当該熱源側膨張弁6により所定の低圧に減圧され、蒸発器として機能する熱源側熱交換器3に流入する。デフロスト運転時には蒸発器として機能する熱源側熱交換器3に流入した冷媒は、送風ファン10の作動により空気と熱交換して気化し、圧縮機2に吸い込まれる。 Further, if the flow of seawater in the inner pipe 11 of the ice maker 1 is blocked and ice is accumulated in the inner pipe 11 (ice accumulation), the ice maker 1 cannot be operated. In this case, a defrost operation (heating operation) is performed to melt the ice in the inner pipe 11. At this time, the four-way switching valve 4 is held in the state shown by the broken line in FIG. The high-temperature and high-pressure gaseous refrigerant discharged from the compressor 2 flows into the annular space between the inner pipe 11 and the outer pipe 12 of the ice maker 1 via the four-way switching valve 4 and the internal heat exchanger 7, and is inside. It condenses and liquefies by exchanging heat with seawater containing ice in the pipe 11. The liquefied refrigerant flows into the heat source side expansion valve 6 via the utilization side expansion valve 5, the internal heat exchanger 7, and the receiver 8 in the fully open state, is depressurized to a predetermined low pressure by the heat source side expansion valve 6, and serves as an evaporator. It flows into the functioning heat source side heat exchanger 3. During the defrost operation, the refrigerant flowing into the heat source side heat exchanger 3 that functions as an evaporator exchanges heat with air by the operation of the blower fan 10, vaporizes, and is sucked into the compressor 2.
 [氷供給装置C]
 氷供給装置Cは、図3に示されるように、製氷装置Iにより生成されたシャーベット氷をユーザに供給する装置である。氷供給装置Cは、シャーベット氷を貯留する貯氷タンクTと、供給路31と、この供給路31に合流する、水が流れる水流路80とを備えている。供給路31は開閉弁を有している。開閉弁を開放することにより、ユーザにシャーベット氷が供給される。本実施形態では、開閉弁は電磁弁37であるが、ユーザが手動で開放する弁等であってもよい。また、氷供給装置Cは、制御部である制御装置25を備えている。制御装置25は、図4に示されるように、CPU25aと、RAM、ROM等のメモリ25bと、外部の機器やセンサ等との受発信を行う受発信部25cとを備えている。制御装置25は、メモリ25bに格納されたコンピュータプログラムをCPU25aが実行することにより、氷供給装置Cの運転制御を含む、製氷システムSの運転に関する種々の制御を実現する。制御装置25は、後述する電磁弁37、73、91、比例制御弁83、及びポンプ32、38等の駆動部ないしアクチュエータの駆動を制御する。また、制御装置25は、温度センサ84、92や水位センサ33からの検知信号を受発信部25cで受信する。また、制御装置25は、製氷装置Iの制御部27と通信可能に接続されており、当該制御部27を経由して製氷装置Iの運転を制御するとともに、当該制御部27を経由して製氷装置Iのセンサ等からの信号を受信する。なお、製氷システムSのメインの制御部を製氷装置I側に付設することもできる。
[Ice supply device C]
As shown in FIG. 3, the ice supply device C is a device that supplies the sherbet ice produced by the ice making device I to the user. The ice supply device C includes an ice storage tank T for storing sherbet ice, a supply path 31, and a water flow path 80 through which water flows, which joins the supply path 31. The supply path 31 has an on-off valve. By opening the on-off valve, sherbet ice is supplied to the user. In the present embodiment, the on-off valve is the solenoid valve 37, but it may be a valve or the like that is manually opened by the user. Further, the ice supply device C includes a control device 25 which is a control unit. As shown in FIG. 4, the control device 25 includes a CPU 25a, a memory 25b such as a RAM and a ROM, and a transmission / reception unit 25c that transmits / receives to / from an external device, a sensor, or the like. The control device 25 realizes various controls related to the operation of the ice making system S, including the operation control of the ice supply device C, by the CPU 25a executing the computer program stored in the memory 25b. The control device 25 controls the drive of the drive units or actuators of the solenoid valves 37, 73, 91, the proportional control valve 83, and the pumps 32, 38, which will be described later. Further, the control device 25 receives the detection signals from the temperature sensors 84 and 92 and the water level sensor 33 at the transmitting / receiving unit 25c. Further, the control device 25 is communicably connected to the control unit 27 of the ice making device I, controls the operation of the ice making device I via the control unit 27, and makes ice via the control unit 27. Receives a signal from the sensor of device I or the like. The main control unit of the ice making system S can be attached to the ice making device I side.
 貯氷タンクTは、ステンレスや鉄等の金属材料で作製されている。貯氷タンクTは水平断面が矩形の角筒形状を呈している。貯氷タンクTは、蓋部を有する密閉された容器であるが、図1及び図3においては、貯氷タンクT内上部の構成を分かり易くするために、当該蓋部の図示は省略している。 The ice storage tank T is made of a metal material such as stainless steel or iron. The ice storage tank T has a rectangular tube shape with a rectangular horizontal cross section. The ice storage tank T is a closed container having a lid portion, but in FIGS. 1 and 3, the lid portion is not shown in order to make it easier to understand the structure of the upper part inside the ice storage tank T.
 貯氷タンクT内の底部近傍には、当該貯氷タンクT内の海水を海水配管15により製氷機1の内管11内に移送するポンプ32が配設されている。底面付近に配置されたポンプ32を駆動して、貯氷タンクT内の海水を製氷機1の内管11内に移送することで、当該貯氷タンクT内のシャーベット氷に流動性を与えることができる。 Near the bottom of the ice storage tank T, a pump 32 for transferring the seawater in the ice storage tank T into the inner pipe 11 of the ice maker 1 by the seawater pipe 15 is arranged. By driving the pump 32 arranged near the bottom surface and transferring the seawater in the ice storage tank T into the inner pipe 11 of the ice maker 1, the sherbet ice in the ice storage tank T can be provided with fluidity. ..
 貯氷タンクT内には水位センサ33が設けられている。この水位センサ33からの検知信号に基づいて、後述する海水の補充や排出が行われる。水位センサ33は、貯氷タンクT内の複数の水位を検知することが可能となっており、例えば、貯氷タンクTの高さの下から90%、70%、45%、30%、25%の位置を検知することができるように配置されている。水位センサ33は、一般的に知られているセンサを用いることができる。また、貯氷タンクTの底部近傍に、当該貯氷タンクT内の海水を排出する排出路90が接続されている。排出路90は電磁弁91を有している。 A water level sensor 33 is provided in the ice storage tank T. Based on the detection signal from the water level sensor 33, seawater is replenished or discharged, which will be described later. The water level sensor 33 can detect a plurality of water levels in the ice storage tank T, for example, 90%, 70%, 45%, 30%, 25% from the bottom of the height of the ice storage tank T. It is arranged so that the position can be detected. As the water level sensor 33, a generally known sensor can be used. Further, a discharge path 90 for discharging seawater in the ice storage tank T is connected near the bottom of the ice storage tank T. The discharge path 90 has a solenoid valve 91.
 供給路31は、製氷装置Iで生成され、貯氷タンクT内に貯留されているシャーベット氷をユーザに供給するための流路又は通路である。供給路31は、下流側端部に、貯氷タンクTから取り出したシャーベット氷を放出する供給口39を有している。供給路31としては、配管、ホース、又はそれらを組み合わせたものを用いることができる。供給路31にはポンプ38が配設されており、このポンプ38を駆動させることで貯氷タンクT内のシャーベット氷を吸引して外部に取り出すことができる。 The supply path 31 is a flow path or aisle for supplying the user with sherbet ice generated by the ice making device I and stored in the ice storage tank T. The supply path 31 has a supply port 39 at the downstream end for discharging the sherbet ice taken out from the ice storage tank T. As the supply path 31, a pipe, a hose, or a combination thereof can be used. A pump 38 is provided in the supply path 31, and by driving the pump 38, sherbet ice in the ice storage tank T can be sucked and taken out to the outside.
 フロート40は、貯氷タンクTの内壁30から離間して当該貯氷タンクT内に浮遊する部材である。本実施形態におけるフロート40は中空体であり、塩化ビニル樹脂(PVC)等の合成樹脂で作製することができる。フロート40は、平面視で正方形状を呈しており、側面視でほぼひし形形状を呈している。より詳細には、フロート40の上面40aは外縁から当該フロート40の中央に向かって液面から遠ざかるように傾斜する上傾斜面を有している。同様に、フロート40の底面40bは外縁から当該フロート40の中央に向かって液面から遠ざかるように傾斜する下傾斜面を有している。なお、フロート40の形状は、本開示において特に限定されず、平面視で円形状を呈するものや、三角形状を呈するものや、五角形以上の多角形状を呈するものを用いることもできる。また、フロート40の上面及び/又は底面を傾斜面とせずに、平坦な面とすることもできる。 The float 40 is a member that floats in the ice storage tank T apart from the inner wall 30 of the ice storage tank T. The float 40 in this embodiment is a hollow body and can be made of a synthetic resin such as vinyl chloride resin (PVC). The float 40 has a square shape in a plan view and a substantially rhombus shape in a side view. More specifically, the upper surface 40a of the float 40 has an upwardly inclined surface that inclines from the outer edge toward the center of the float 40 so as to move away from the liquid surface. Similarly, the bottom surface 40b of the float 40 has a downwardly sloping surface that slopes away from the liquid surface from the outer edge toward the center of the float 40. The shape of the float 40 is not particularly limited in the present disclosure, and a float 40 having a circular shape, a triangular shape, or a polygonal shape having a pentagon or more can be used. Further, the upper surface and / or the bottom surface of the float 40 may be a flat surface instead of an inclined surface.
 フロート40のサイズは、本開示において特に限定されないが、平面視で内壁が矩形状の貯氷タンクT内に平面視が正方形のフロート40を浮かべる場合、貯氷タンクTの1辺の長さ(短い方の長さ)をWとすると、正方形のフロート40の1辺の長さを例えば0.3~0.5Wとすることができる。また、平面視が円形の貯氷タンクT内に平面視が円形のフロート40を浮かべる場合、貯氷タンクTの内径をDとすると、円形のフロート40の外径を例えば0.3~0.5Dとすることができる。 The size of the float 40 is not particularly limited in the present disclosure, but when the float 40 having a square inner wall is floated in the ice storage tank T having a rectangular inner wall in a plan view, the length of one side of the ice storage tank T (the shorter one). The length of one side of the square float 40 can be, for example, 0.3 to 0.5 W. Further, when the float 40 having a circular plan view is floated in the ice storage tank T having a circular plan view, if the inner diameter of the ice storage tank T is D, the outer diameter of the circular float 40 is, for example, 0.3 to 0.5 D. can do.
 フロート40の中央(平面視における中央)には上下方向に貫通する開口41が形成されている。この開口41は平面視で円形状である。本実施形態では、供給路31の一部を構成するホース34の先端部34aが開口41内に挿入されてフロート40に固定されている。ホース34は、先端部34aの根元側に蛇腹部34bを有している。この蛇腹部34bは、ホース34の長手方向又は軸方向に沿って所定距離だけ伸縮自在である。また、蛇腹部34bの先端部34aと反対側の端部は供給路31を構成する配管35の端部の拡径部35aに接続されている。この配管35は、図示しない固定具によってその位置が固定されている。 An opening 41 penetrating in the vertical direction is formed in the center of the float 40 (center in a plan view). The opening 41 has a circular shape in a plan view. In the present embodiment, the tip 34a of the hose 34 forming a part of the supply path 31 is inserted into the opening 41 and fixed to the float 40. The hose 34 has a bellows portion 34b on the root side of the tip portion 34a. The bellows portion 34b can be expanded and contracted by a predetermined distance along the longitudinal direction or the axial direction of the hose 34. Further, the end portion of the bellows portion 34b opposite to the tip portion 34a is connected to the diameter-expanded portion 35a of the end portion of the pipe 35 constituting the supply path 31. The position of the pipe 35 is fixed by a fixture (not shown).
 正方形状のフロート40の4つの角部にはそれぞれチェーン36の一端が固定されている。チェーン36の他端は貯氷タンクTの内壁30に係止されている。各チェーン36の長さは、フロート40一定範囲内の上下動及び水平移動を許容する長さに設定されている。フロート40は、蛇腹部34bの存在により一定の範囲内で上下動が可能である。また、フロート40は、チェーン36の存在により一定の範囲を超える水平移動が規制される。 One end of the chain 36 is fixed to each of the four corners of the square float 40. The other end of the chain 36 is locked to the inner wall 30 of the ice storage tank T. The length of each chain 36 is set to a length that allows vertical movement and horizontal movement within a certain range of the float 40. The float 40 can move up and down within a certain range due to the presence of the bellows portion 34b. Further, the float 40 is restricted from moving horizontally beyond a certain range due to the presence of the chain 36.
 本実施形態では、前述した配管35、ホース34及び開口41により供給路31が構成されている。供給路31の先端部であるフロート40の開口41の先端(開口縁)が、貯氷タンクT内に貯留されているシャーベット氷を吸引して取り出すための取出口42として機能する。この取出口42は、フロート40の底面40bに位置している。換言すれば、取出口42は、タンク本体内に貯留されているシャーベット氷の液面下に位置している。取出口42の上下方向の位置は、本開示において特に限定されないが、例えばシャーベット氷の液面Lより10~40cm程度下方に位置するようにフロート40のサイズ、形状及び重量等を選定することができる。 In the present embodiment, the supply path 31 is configured by the above-mentioned pipe 35, hose 34, and opening 41. The tip (opening edge) of the opening 41 of the float 40, which is the tip of the supply path 31, functions as an outlet 42 for sucking and taking out the sherbet ice stored in the ice storage tank T. The outlet 42 is located on the bottom surface 40b of the float 40. In other words, the outlet 42 is located below the surface of the sherbet ice stored in the tank body. The vertical position of the outlet 42 is not particularly limited in the present disclosure, but for example, the size, shape, weight, etc. of the float 40 may be selected so as to be located about 10 to 40 cm below the liquid level L of the sherbet ice. it can.
 氷は海水よりも比重が小さいことから浮力により上方に移動するので、貯氷タンクT内において液面付近のシャーベット氷は底面付近のシャーベット氷よりも高いIPFを有している。本実施形態では、供給路31の先端部の取出口42が、貯氷タンクTの上下方向において下部や中央部ではなく、その上部に配置されているので、IPFが高いシャーベット氷をユーザに供給することができる。その際、供給路31の先端部の取出口42がシャーベット氷の液面下に配置されているので、取出口42からシャーベット氷を吸引するに際し当該取出口42から空気が吸い込まれるのを抑制することができる。そして、吸い込まれた空気によってポンプ38が破損するのを抑制することができる。 Since ice has a lower specific density than seawater, it moves upward due to buoyancy, so sherbet ice near the liquid surface in the ice storage tank T has a higher IPF than sherbet ice near the bottom surface. In the present embodiment, since the outlet 42 at the tip of the supply path 31 is arranged not at the lower part or the central part in the vertical direction of the ice storage tank T but at the upper part thereof, sherbet ice having a high IPF is supplied to the user. be able to. At that time, since the outlet 42 at the tip of the supply path 31 is arranged below the liquid level of the sherbet ice, it is possible to suppress the suction of air from the outlet 42 when sucking the sherbet ice from the outlet 42. be able to. Then, it is possible to prevent the pump 38 from being damaged by the sucked air.
 また、フロート40の底面40bは、当該フロート40の外縁から取出口42に向かって液面から遠ざかるように傾斜する下傾斜面を有しているので、当該取出口42周辺の液中の空気を前記傾斜面に沿って上方に逃がすことができる。これにより、供給路31の先端部の取出口42からの空気の吸い込みをさらに抑制することができる。 Further, since the bottom surface 40b of the float 40 has a downwardly inclined surface that inclines from the outer edge of the float 40 toward the outlet 42 so as to move away from the liquid surface, the air in the liquid around the outlet 42 can be removed. It can escape upward along the inclined surface. As a result, the suction of air from the outlet 42 at the tip of the supply path 31 can be further suppressed.
 本実施形態に係る氷供給装置Cは、供給路31に配設されたポンプ38の下流側において当該供給路31から分岐しており、貯氷タンクTにシャーベット氷を戻す還流路50を有している。還流路50は、製氷機1で生成された氷を含む海水を貯氷タンクTに戻すシャーベット配管16に接続されている。また、還流路50には安全弁51が配設されている。この安全弁51は、還流路50内の圧力が所定圧を超えて大きくなったときに、開放する。また、安全弁51は、供給路31に設けられた電磁弁37が故障し、供給口39からシャーベット氷の供給ができなくなったにもかかわらずポンプ38が駆動している場合に、当該供給路31から分岐している還流路50内の圧力が所定圧を超えて大きくなったときに、開放して、シャーベット氷を貯氷タンクT内に戻す役割も果たしている。このシャーベット氷は、貯氷タンクT内に貯留されているシャーベット氷の液面Lの上方に配設されている、後述する放出管の放出口から落下するので、液面付近のシャーベット氷を乱すことができる。また、シャーベット氷が凍結するのを抑制することができる。また、安全弁51が開放してシャーベット氷の流路内の圧力を下げることで、過大圧力によりポンプ38が故障するのを回避することができる。 The ice supply device C according to the present embodiment has a return path 50 that branches off from the supply path 31 on the downstream side of the pump 38 arranged in the supply path 31 and returns sherbet ice to the ice storage tank T. There is. The return passage 50 is connected to a sherbet pipe 16 that returns seawater containing ice generated by the ice maker 1 to the ice storage tank T. Further, a safety valve 51 is provided in the return passage 50. The safety valve 51 is opened when the pressure in the return passage 50 exceeds a predetermined pressure. Further, the safety valve 51 is used when the pump 38 is driven even though the solenoid valve 37 provided in the supply path 31 has failed and the sherbet ice cannot be supplied from the supply port 39. When the pressure in the return passage 50 branching from the above exceeds a predetermined pressure, it is released to return the sherbet ice to the ice storage tank T. This sherbet ice falls from the discharge port of the discharge pipe described later, which is arranged above the liquid level L of the sherbet ice stored in the ice storage tank T, and therefore disturbs the sherbet ice near the liquid level. Can be done. In addition, it is possible to prevent the sherbet ice from freezing. Further, by opening the safety valve 51 to reduce the pressure in the flow path of the sherbet ice, it is possible to prevent the pump 38 from failing due to excessive pressure.
 なお、安全弁51に代えて開閉制御可能な電磁弁を用いることもできる。この場合、電磁弁は、制御装置25のCPU25aにより、供給路31の供給口39によってシャーベット氷のユーザへの供給が行われている場合に閉となるように制御され、供給路31の供給口39からシャーベット氷の供給が行われていない場合に開となるように制御される。シャーベット氷の供給が行われていない場合に、ポンプ38を作動させるとともに電磁弁が開となるように制御することで、シャーベット氷を貯氷タンクT内に戻すことができる。これにより、貯氷タンクT内に貯留されているシャーベット氷に流動性を与え、当該シャーベット氷が凍結するのを抑制することができる。 A solenoid valve that can be opened and closed can be used instead of the safety valve 51. In this case, the solenoid valve is controlled by the CPU 25a of the control device 25 so as to be closed when the sherbet ice is supplied to the user by the supply port 39 of the supply path 31, and the supply port of the supply path 31 is closed. From 39, it is controlled to open when the sherbet ice is not supplied. When the sherbet ice is not supplied, the sherbet ice can be returned to the ice storage tank T by operating the pump 38 and controlling the solenoid valve to open. As a result, it is possible to impart fluidity to the sherbet ice stored in the ice storage tank T and prevent the sherbet ice from freezing.
 供給路31に配設されたポンプ38は、貯氷タンクT内のシャーベット氷を供給口39よりユーザに供給するためのポンプとして機能するとともに、当該供給路31から分岐する還流路50を介して貯氷タンクTから取り出したシャーベット氷を当該貯氷タンクTに戻すためのポンプとして機能することができる。シャーベット氷の供給用ポンプと還流用ポンプを共用化することができる。 The pump 38 arranged in the supply path 31 functions as a pump for supplying the sherbet ice in the ice storage tank T to the user from the supply port 39, and also stores ice via the reflux path 50 branching from the supply path 31. It can function as a pump for returning the sherbet ice taken out from the tank T to the ice storage tank T. The sherbet ice supply pump and the reflux pump can be shared.
 制御装置25のCPU25aにより、ポンプ38の運転と、前述した開閉制御可能な電磁弁の開閉制御とを、連動させることで、貯氷タンクT内のシャーベット氷が凍結するのを抑制することができる。具体的に、製氷装置Iが運転している間、常時又は定期的にポンプ38を駆動させることで、常に又は定期的に貯氷タンクT内のシャーベット氷を還流路に流して循環させることができ、これにより製氷中に液面付近のシャーベット氷が凍結するのを抑制することができる。電磁弁の開閉は、ポンプ38の駆動と連動するように制御装置25のCPU25aにより制御される。なお、製氷装置Iが運転していないときに、常に又は定期的に貯氷タンクT内のシャーベット氷を還流路に流して循環させることにより、貯氷タンクT内のシャーベット氷が凍結することを抑制することもできる。 By linking the operation of the pump 38 with the opening / closing control of the solenoid valve capable of opening / closing control described above by the CPU 25a of the control device 25, it is possible to suppress freezing of the sherbet ice in the ice storage tank T. Specifically, by driving the pump 38 constantly or periodically while the ice making device I is operating, the sherbet ice in the ice storage tank T can be constantly or periodically flowed through the return path and circulated. As a result, it is possible to prevent the sherbet ice near the liquid surface from freezing during ice making. The opening and closing of the solenoid valve is controlled by the CPU 25a of the control device 25 so as to be interlocked with the drive of the pump 38. When the ice making device I is not in operation, the sherbet ice in the ice storage tank T is prevented from freezing by constantly or periodically flowing the sherbet ice in the ice storage tank T through the reflux path and circulating the ice. You can also do it.
 シャーベット配管16の下流側の端部は、図5に示されるように、4本の枝管60に分岐している。各枝管60の下流側の端部には放出管61が取り付けられている。放出管61の下面には複数(図5に示される例では6個)の放出口62が形成されている。枝管60及び放出管61は、貯氷タンクT内に貯留されているシャーベット氷の液面Lよりも上方に配置されている。シャーベット氷の液面Lより上方に位置する放出口62からシャーベット氷を落下させることで、液面付近のシャーベット氷に流動性を与えることができる。これにより、液面付近のシャーベット氷が凍結するのを抑制することができる。 The downstream end of the sherbet pipe 16 is branched into four branch pipes 60 as shown in FIG. A discharge pipe 61 is attached to the downstream end of each branch pipe 60. A plurality of (six in the example shown in FIG. 5) discharge ports 62 are formed on the lower surface of the discharge pipe 61. The branch pipe 60 and the discharge pipe 61 are arranged above the liquid level L of the sherbet ice stored in the ice storage tank T. By dropping the sherbet ice from the discharge port 62 located above the liquid level L of the sherbet ice, it is possible to impart fluidity to the sherbet ice near the liquid surface. As a result, it is possible to prevent the sherbet ice near the liquid surface from freezing.
 本実施形態では、貯氷タンクTに海水を補給する海水補給管70の下流側の端部がシャーベット配管16に接続されている。図示しないポンプにより海水取得口から吸引された海水は、殺菌・ろ過装置72、及び電磁弁73を経由してシャーベット配管16に合流し、前述した放出管61の放出口62から貯氷タンクTに供給される。殺菌・ろ過装置72は、海水に含まれている異物を除去したり、海水中に含まれる菌を滅菌したりするための装置である。海水補給管70を用いた海水の貯氷タンクTへの補給は、前述した水位センサ33の検知信号に基づいて行うことができる。 In the present embodiment, the downstream end of the seawater supply pipe 70 that supplies seawater to the ice storage tank T is connected to the sherbet pipe 16. The seawater sucked from the seawater acquisition port by a pump (not shown) joins the sherbet pipe 16 via the sterilization / filtration device 72 and the solenoid valve 73, and is supplied to the ice storage tank T from the discharge port 62 of the discharge pipe 61 described above. Will be done. The sterilization / filtration device 72 is a device for removing foreign substances contained in seawater and sterilizing bacteria contained in seawater. The seawater can be replenished to the ice storage tank T using the seawater replenishment pipe 70 based on the detection signal of the water level sensor 33 described above.
 また、本実施形態に係る氷供給装置Cは、貯氷タンクTからシャーベット氷を取り出す供給路31に合流する、水が流れる水流路80を有している。この水流路80は、貯氷タンクTからシャーベット氷を吸引して取り出すためのポンプ38よりもシャーベット氷の流れ方向上流側において供給路31に合流している。これにより、2台必要であったポンプの数を1台に減らすことができる。なお、水に代えて、水に塩分を含有した塩水を用いることもできる。 Further, the ice supply device C according to the present embodiment has a water flow path 80 through which water flows, which joins the supply path 31 for taking out sherbet ice from the ice storage tank T. The water flow path 80 joins the supply path 31 on the upstream side in the flow direction of the sherbet ice with respect to the pump 38 for sucking and taking out the sherbet ice from the ice storage tank T. As a result, the number of pumps required for two can be reduced to one. In addition, instead of water, salt water containing salt in water can also be used.
 本実施形態では、制御装置25に通信可能に接続された入力部26(図4参照)が設けられている。ユーザは、貯氷タンクTから取り出すシャーベット氷の塩分濃度及び量を入力することで、所望の塩分濃度を有するシャーベット氷を所望の量だけ供給口39から取り出すことができる。 In the present embodiment, an input unit 26 (see FIG. 4) that is communicably connected to the control device 25 is provided. By inputting the salt concentration and amount of sherbet ice to be taken out from the ice storage tank T, the user can take out a desired amount of sherbet ice having a desired salt concentration from the supply port 39.
 本実施形態では、水タンク81に貯留されている水はポンプ38により吸引され、流量調整弁である比例制御弁83を経由して供給路31に合流する。また、水流路80と供給路31との合流部よりも下流側であり且つポンプ38の下流側にシャーベット氷の温度を検知する、第1温度センサである温度センサ84が設けられている。シャーベット氷の塩分濃度と温度の間には相関関係が存在するので、温度センサ84によりシャーベット氷の温度を検出することで、検出した温度から塩分濃度を演算することができる。この演算は、制御装置25のCPU25aで行うことができる。そして、演算された塩分濃度に基づいて、当該塩分濃度が目標値となるように制御装置25のCPU25aによって比例制御弁83の開度及び/又は開時間を調整することで、所望の塩分濃度を有するシャーベット氷を得ることができる。例えば、比例制御弁83の開度を全開とした場合、供給路31を流れるシャーベット氷の流量と水流路80を流れる流量がほぼ等しくなるように構成されている。これにより、電磁弁37から取り出すシャーベット氷の濃度を、貯氷タンクT内に貯留されているシャーベット氷の濃度の約半分の濃度とすることができる。また、例えば、比例制御弁83の開度を50%とした場合、供給路31を流れるシャーベット氷の流量と水流路80を流れる流量の比が、2対1となる。これにより、電磁弁37から取り出すシャーベット氷の濃度を、貯氷タンクT内に貯留されているシャーベット氷の濃度の約3分の2とすることができる。また、比例制御弁83を全開とする時間を、ポンプ38を運転している時間のうちの約半分の時間とした場合、電磁弁37から取り出すシャーベット氷の濃度を、貯氷タンクT内に貯留されているシャーベット氷の濃度の約3分の2とすることができる。なお、温度センサ84に代えて塩分濃度を検出する濃度センサ84(第1濃度センサ)を用いてもよい。この場合、検出された塩分濃度に基づいて、当該塩分濃度が目標値となるように制御装置25によって比例制御弁83の開度及び/又は開時間を調整することができる。 In the present embodiment, the water stored in the water tank 81 is sucked by the pump 38 and joins the supply path 31 via the proportional control valve 83 which is a flow rate adjusting valve. Further, a temperature sensor 84, which is a first temperature sensor, is provided on the downstream side of the confluence of the water flow path 80 and the supply path 31 and on the downstream side of the pump 38 to detect the temperature of sherbet ice. Since there is a correlation between the salt concentration of sherbet ice and the temperature, the salt concentration can be calculated from the detected temperature by detecting the temperature of the sherbet ice with the temperature sensor 84. This calculation can be performed by the CPU 25a of the control device 25. Then, based on the calculated salt concentration, the opening and / or opening time of the proportional control valve 83 is adjusted by the CPU 25a of the control device 25 so that the salt concentration becomes the target value, thereby adjusting the desired salt concentration. You can get sherbet ice to have. For example, when the opening degree of the proportional control valve 83 is fully opened, the flow rate of sherbet ice flowing through the supply path 31 and the flow rate flowing through the water flow path 80 are configured to be substantially equal to each other. As a result, the concentration of sherbet ice taken out from the solenoid valve 37 can be set to about half the concentration of sherbet ice stored in the ice storage tank T. Further, for example, when the opening degree of the proportional control valve 83 is set to 50%, the ratio of the flow rate of sherbet ice flowing through the supply path 31 to the flow rate flowing through the water flow path 80 is 2: 1. As a result, the concentration of sherbet ice taken out from the solenoid valve 37 can be reduced to about two-thirds of the concentration of sherbet ice stored in the ice storage tank T. Further, when the time for fully opening the proportional control valve 83 is set to about half the time during which the pump 38 is operated, the concentration of sherbet ice taken out from the electromagnetic valve 37 is stored in the ice storage tank T. It can be about two-thirds of the concentration of sherbet ice. Instead of the temperature sensor 84, a concentration sensor 84 (first concentration sensor) that detects the salt concentration may be used. In this case, the opening degree and / or opening time of the proportional control valve 83 can be adjusted by the control device 25 so that the salt concentration becomes a target value based on the detected salt concentration.
 また、本実施形態では、貯氷タンクT内に当該貯氷タンクT内のシャーベット氷の温度を検出する、第2温度センサである温度センサ92が配設されている。この温度センサ92により検出される運転前の海水の温度及び運転開始後のシャーベット氷の温度に基づいて、制御装置25のCPU25aによって当該シャーベット氷の塩分濃度を求めることができる。そして、制御装置25のCPU25aは、塩分濃度に基づいて、比例制御弁83の開度及び/又は開時間を変化させることにより、水流路80から供給路31に合流させる水の流量を調整する。これにより、ユーザに供給されるシャーベット氷の塩分濃度を調整することができる。なお、第2温度センサである温度センサ92の代わりに、第2濃度センサである濃度センサ92を用いることも可能である。この場合、制御装置25のCPU25aは、当該貯氷タンクT内のシャーベット氷の濃度を、濃度センサ92により得ることができる。 Further, in the present embodiment, a temperature sensor 92, which is a second temperature sensor, is provided in the ice storage tank T to detect the temperature of the sherbet ice in the ice storage tank T. Based on the temperature of seawater before operation and the temperature of sherbet ice after the start of operation detected by the temperature sensor 92, the salt concentration of the sherbet ice can be determined by the CPU 25a of the control device 25. Then, the CPU 25a of the control device 25 adjusts the flow rate of water merging from the water flow path 80 to the supply path 31 by changing the opening degree and / or opening time of the proportional control valve 83 based on the salinity. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user. It is also possible to use the concentration sensor 92, which is the second concentration sensor, instead of the temperature sensor 92, which is the second temperature sensor. In this case, the CPU 25a of the control device 25 can obtain the concentration of sherbet ice in the ice storage tank T by the concentration sensor 92.
 また、シャーベット氷の塩分濃度と温度との間には相関関係が存在するので、温度センサ92でシャーベット氷の温度を検出することで、当該検出した温度から制御装置25のCPU25aで塩分濃度を演算することができる。そして、制御装置25のCPU25aは、演算された塩分濃度が所定範囲内でない場合、貯氷タンクT内のシャーベット氷の取出操作を禁止する。貯氷タンクT内のシャーベット氷の塩分濃度が低すぎる場合、当該シャーベット氷のIPFも低く、シャーベット氷としての利用が不十分である。検出された塩分濃度が所定範囲内でない場合に、貯氷タンク内のシャーベット氷の取出操作を禁止することで、ユーザに不十分な状態のシャーベット氷が供給されるのを抑制することができる。なお、第2温度センサである温度センサ92の代わりに、第2濃度センサである濃度センサ92を用いる場合、制御装置25のCPU25aは、濃度センサ92により検出されたシャーベット氷の塩分濃度が所定範囲でない場合、貯氷タンクT内のシャーベット氷の取出操作を禁止する。 Further, since there is a correlation between the salt concentration of sherbet ice and the temperature, the temperature of the sherbet ice is detected by the temperature sensor 92, and the salt concentration is calculated by the CPU 25a of the control device 25 from the detected temperature. can do. Then, the CPU 25a of the control device 25 prohibits the operation of taking out the sherbet ice in the ice storage tank T when the calculated salt concentration is not within the predetermined range. If the salt concentration of the sherbet ice in the ice storage tank T is too low, the IPF of the sherbet ice is also low, and the use as sherbet ice is insufficient. By prohibiting the operation of taking out the sherbet ice in the ice storage tank when the detected salt concentration is not within the predetermined range, it is possible to suppress the supply of the sherbet ice in an insufficient state to the user. When the concentration sensor 92, which is the second concentration sensor, is used instead of the temperature sensor 92, which is the second temperature sensor, the CPU 25a of the control device 25 has a predetermined range of the salt concentration of the sherbet ice detected by the concentration sensor 92. If not, the operation of taking out the sherbet ice in the ice storage tank T is prohibited.
 本実施形態では、制御装置25のCPU25aは、温度センサ92により検出された温度に基づいて算出された塩分濃度が所定値を超えていると判断すると、電磁弁91と電磁弁73を制御する。具体的に、制御装置25のCPU25aは、算出された塩分濃度が所定値を超えた場合、電磁弁91を開放する。これにより、貯氷タンクT内の海水を排出路90を経由して外部に排出する。そして、第1所定条件が満たされると、CPU25aは電磁弁91を閉止し、その後電磁弁73を開放して貯氷タンクTに海水を供給する。そして、第2所定条件が満たされると、CPU25aは、電磁弁73を閉止する。このように、貯氷タンクT内の海水の塩分濃度に基づいて当該貯氷タンクT内の海水の排出及び当該貯氷タンクTへの海水の供給を行うことで、貯氷タンクT内の海水の塩分濃度を所定値未満に下げることができ、その結果、製氷装置Iを連続して運転することができる。これにより、製氷システムSの製氷効率を向上させることができる。なお、貯氷タンクT内の海水の濃度を検出する手段として、塩分濃度センサを用いることもできる。 In the present embodiment, the CPU 25a of the control device 25 controls the solenoid valve 91 and the solenoid valve 73 when it is determined that the salt concentration calculated based on the temperature detected by the temperature sensor 92 exceeds a predetermined value. Specifically, the CPU 25a of the control device 25 opens the solenoid valve 91 when the calculated salt concentration exceeds a predetermined value. As a result, the seawater in the ice storage tank T is discharged to the outside via the discharge path 90. Then, when the first predetermined condition is satisfied, the CPU 25a closes the solenoid valve 91, then opens the solenoid valve 73 to supply seawater to the ice storage tank T. Then, when the second predetermined condition is satisfied, the CPU 25a closes the solenoid valve 73. In this way, by discharging the seawater in the ice storage tank T and supplying the seawater to the ice storage tank T based on the salt concentration of the seawater in the ice storage tank T, the salt concentration of the seawater in the ice storage tank T can be increased. The value can be lowered below a predetermined value, and as a result, the ice making device I can be continuously operated. Thereby, the ice making efficiency of the ice making system S can be improved. A salinity sensor can also be used as a means for detecting the concentration of seawater in the ice storage tank T.
 前述した「所定値」は、本開示において特に限定されないが、例えば7%とすることができる。貯氷タンクT内のシャーベット氷の塩分濃度が7%を超えると、製氷機1における製氷が難しくなり製氷効率が低下する恐れがある。所定値は、図示しない制御装置25の入力部を介して、適宜設定することが可能である。設定された所定値は、メモリ25bに記憶される。また、「第1所定条件」及び「第2所定条件」としては、例えば水と氷との分かれ目としての水位が一定位置まで下がったときとすることができる。第1所定条件では、制御装置25のCPU25aは、水位が第1位置まで下がったことを、水位センサ33により検知する。第1位置としては、例えば、前述した水位センサ33により検知される複数の水位のうち、タンク高さの下から45%の位置を選択することができる。氷だけを扱うとポンプが破損する可能性があることから、前述した水位が第1位置まで下がると、排水を止めて給水を始めるように構成されている。また、第2所定条件では、制御装置25のCPU25aは、水位が第2位置まで上がったことを、水位センサ33により検知する。第2位置としては、例えば、前述した水位センサ33により検知される複数の水位のうち、タンク高さの下から90%の位置を選択することができる。第1位置および第2位置は、図示しない制御装置25の入力部を介して、適宜設定することが可能である。設定された第1位置および第2位置は、メモリ25bに記憶される。本実施形態では、図6に示されるように、以下の様な制御フローが実行されている。制御装置25のCPU25aは、貯氷タンクT内に配設された温度センサ92により当該貯氷タンクT内のシャーベット氷の塩分濃度を検知する(ステップS1)。制御装置25のCPU25aは、当該塩分濃度が7%を超えているか否かを判断し(ステップS2)、塩分濃度が7%を超えていると判断するとステップS3に処理を進める。ステップS3で、CPU25aは、製氷装置Iの制御部27に対して、製氷装置Iの運転を停止するよう指令を送信する。CPU25aは、貯氷タンクTに接続されている排出路90に設けられた電磁弁91を開放する(ステップS4)。これにより、貯氷タンクTの底面付近の海水が排出される。なお、排出される海水は、多少シャーベット氷を含有していることもある。 The above-mentioned "predetermined value" is not particularly limited in the present disclosure, but can be, for example, 7%. If the salt concentration of the sherbet ice in the ice storage tank T exceeds 7%, it becomes difficult to make ice in the ice making machine 1, and the ice making efficiency may decrease. The predetermined value can be appropriately set via an input unit of a control device 25 (not shown). The set predetermined value is stored in the memory 25b. Further, the "first predetermined condition" and the "second predetermined condition" can be, for example, when the water level as a dividing line between water and ice drops to a certain position. Under the first predetermined condition, the CPU 25a of the control device 25 detects that the water level has dropped to the first position by the water level sensor 33. As the first position, for example, a position 45% from the bottom of the tank height can be selected from the plurality of water levels detected by the water level sensor 33 described above. Since the pump may be damaged if only ice is handled, the pump is configured to stop drainage and start water supply when the water level described above drops to the first position. Further, under the second predetermined condition, the CPU 25a of the control device 25 detects that the water level has risen to the second position by the water level sensor 33. As the second position, for example, 90% of the positions of the plurality of water levels detected by the water level sensor 33 described above can be selected from the bottom of the tank height. The first position and the second position can be appropriately set via an input unit of a control device 25 (not shown). The set first position and second position are stored in the memory 25b. In this embodiment, as shown in FIG. 6, the following control flow is executed. The CPU 25a of the control device 25 detects the salt concentration of the sherbet ice in the ice storage tank T by the temperature sensor 92 arranged in the ice storage tank T (step S1). The CPU 25a of the control device 25 determines whether or not the salt concentration exceeds 7% (step S2), and if it determines that the salt concentration exceeds 7%, proceeds to step S3. In step S3, the CPU 25a transmits a command to the control unit 27 of the ice making device I to stop the operation of the ice making device I. The CPU 25a opens the solenoid valve 91 provided in the discharge path 90 connected to the ice storage tank T (step S4). As a result, seawater near the bottom surface of the ice storage tank T is discharged. The discharged seawater may contain some sherbet ice.
 ついでCPU25aは、ステップS5において、水位センサ33により検知される水位が、第1所定条件より低い水位まで下がったか否かを判断する。CPU25aは、ステップS5において、水位が、第1所定条件より低い水位まで下がったと判断すると、ステップS6に処理を進め、当該ステップS6において電磁弁91を閉止する。次に、CPU25aは、電磁弁73を開放する(ステップS7)。これにより、海水(塩分濃度約3.5%)が貯氷タンクT内に供給される。ついでCPU25aは、ステップS8において、水位センサ33により検知される水位が、第2所定条件より高い水位まで上がったか否かを判断する。CPU25aは、ステップS8において、水位が、第2所定条件より高い水位まで上がったと判断すると、ステップS9に処理を進め、当該ステップS9において電磁弁73を閉止する。その後、CPU25aは、ステップS10において、製氷装置Iの制御部に対して、製氷装置Iの運転を開始させる指令を送信する。ステップS10を行った後、ステップS1へ戻り、制御装置25のCPU25aは、貯氷タンクT内に配設された温度センサ92により当該貯氷タンクT内のシャーベット氷の塩分濃度の検知を行う。このようなステップS1からステップS10を繰り返すことによって、製氷装置Iを連続して運転することができる。貯氷タンクT内の目標塩分濃度としては、例えば3.5~7%とすることができる。このような制御を行うことにより、製氷装置Iを連続して運転することができる。 Then, in step S5, the CPU 25a determines whether or not the water level detected by the water level sensor 33 has dropped to a water level lower than the first predetermined condition. When the CPU 25a determines in step S5 that the water level has dropped to a water level lower than the first predetermined condition, the CPU 25a proceeds to step S6 and closes the solenoid valve 91 in step S6. Next, the CPU 25a opens the solenoid valve 73 (step S7). As a result, seawater (salt concentration of about 3.5%) is supplied into the ice storage tank T. Then, in step S8, the CPU 25a determines whether or not the water level detected by the water level sensor 33 has risen to a water level higher than the second predetermined condition. When the CPU 25a determines in step S8 that the water level has risen to a level higher than the second predetermined condition, the CPU 25a proceeds to step S9 and closes the solenoid valve 73 in step S9. After that, in step S10, the CPU 25a transmits a command to start the operation of the ice making device I to the control unit of the ice making device I. After performing step S10, the process returns to step S1, and the CPU 25a of the control device 25 detects the salt concentration of the sherbet ice in the ice storage tank T by the temperature sensor 92 arranged in the ice storage tank T. By repeating such steps S1 to S10, the ice making device I can be continuously operated. The target salt concentration in the ice storage tank T can be, for example, 3.5 to 7%. By performing such control, the ice making device I can be continuously operated.
 なお、温度センサ92により検出された貯氷タンクTの海水の塩分濃度が所定値を超えた場合、制御装置25のCPU25aは、当該貯氷タンクT内の海水の塩分濃度が目標塩分濃度となるように、排出路90の電磁弁91及び海水補給管70の電磁弁73を制御するようにしてもよい。この場合の制御としては、以下のように制御することができる。制御装置25のCPU25aは、海水補給管70より供給される海水の塩分濃度を認識している。制御装置25のCPU25aは、貯氷タンクT内の海水の塩分濃度が所定値となったときに、貯氷タンクTから排出する海水の量および海水補給管70から供給される海水の量を演算することによって、貯氷タンクT内で異なる濃度の塩水が混ざったときの塩分濃度が目標塩分濃度となるように、電磁弁91及び電磁弁73を制御することができる。この場合、第1所定条件は、貯氷タンクTから排出する海水の量とすることができ、第2所定条件は、海水補給管70から供給される海水の量とすることができる。 When the salt concentration of the seawater in the ice storage tank T detected by the temperature sensor 92 exceeds a predetermined value, the CPU 25a of the control device 25 sets the salt concentration of the seawater in the ice storage tank T to the target salt concentration. , The solenoid valve 91 of the discharge path 90 and the solenoid valve 73 of the seawater supply pipe 70 may be controlled. The control in this case can be controlled as follows. The CPU 25a of the control device 25 recognizes the salt concentration of the seawater supplied from the seawater supply pipe 70. The CPU 25a of the control device 25 calculates the amount of seawater discharged from the ice storage tank T and the amount of seawater supplied from the seawater supply pipe 70 when the salt concentration of the seawater in the ice storage tank T reaches a predetermined value. Therefore, the electromagnetic valve 91 and the electromagnetic valve 73 can be controlled so that the salt concentration when different concentrations of salt water are mixed in the ice storage tank T becomes the target salt concentration. In this case, the first predetermined condition can be the amount of seawater discharged from the ice storage tank T, and the second predetermined condition can be the amount of seawater supplied from the seawater supply pipe 70.
 水タンク81には制御弁86を経由して水が供給される。水タンク81内にはフロートスイッチ87が配置されており、このフロートスイッチ87からの検知信号に基づいて制御弁86が開閉制御され、水タンク81への水の供給の開始及び停止操作が行われる。 Water is supplied to the water tank 81 via the control valve 86. A float switch 87 is arranged in the water tank 81, and the control valve 86 is controlled to open and close based on the detection signal from the float switch 87, and the water supply to the water tank 81 is started and stopped. ..
[第1の実施形態の作用効果]
 前述した第1の実施形態(氷供給装置の実施形態)では、貯氷タンクTからシャーベット氷を取り出す供給路31に、水が流れる水流路80が合流している。これにより、供給路31に合流させる水の流量を調整することでユーザに供給されるシャーベット氷の塩分濃度を容易に調整することができる。所定量のシャーベット氷をユーザに供給した後に、例えば、種類が異なる海水魚を保冷するためのシャーベット氷が必要になったときでも、供給路31に合流させる水流路80からの水の流量を調整するだけでシャーベット氷の塩分濃度を調整することができるので、氷供給装置Cの使い勝手がよくなる。
[Action and effect of the first embodiment]
In the first embodiment described above (the embodiment of the ice supply device), the water flow path 80 through which water flows joins the supply path 31 for taking out sherbet ice from the ice storage tank T. Thereby, the salt concentration of the sherbet ice supplied to the user can be easily adjusted by adjusting the flow rate of the water merging into the supply path 31. After supplying a predetermined amount of sherbet ice to the user, for example, even when sherbet ice for cooling different types of saltwater fish is needed, the flow rate of water from the water flow path 80 to be merged with the supply path 31 is adjusted. Since the salt concentration of the sherbet ice can be adjusted simply by doing so, the usability of the ice supply device C is improved.
 また、前述した第1の実施形態では、水流路80が供給路31に合流する合流部よりも、シャーベット氷の流れ方向下流側にポンプ38が配設されている。合流部よりも、シャーベット氷の流れ方向下流側にポンプ38を配設することで、1台のポンプでシャーベット氷と水を流動させることができる。 Further, in the first embodiment described above, the pump 38 is arranged on the downstream side in the flow direction of the sherbet ice from the confluence portion where the water flow path 80 merges with the supply path 31. By disposing the pump 38 on the downstream side in the flow direction of the sherbet ice from the confluence portion, the sherbet ice and water can be flowed by one pump.
 また、前述した第1の実施形態では、水流路80に比例制御弁83が配設されており、合流後のシャーベット氷の塩分濃度が目標値となるように、制御装置25のCPU25aによって比例制御弁83の開度及び/又は開時間が制御される。水流路80に設けられた比例制御弁83の開度及び/又は開時間を制御するだけで合流後のシャーベット氷の塩分濃度を調整することができる。 Further, in the first embodiment described above, the proportional control valve 83 is provided in the water flow path 80, and proportional control is performed by the CPU 25a of the control device 25 so that the salt concentration of the sherbet ice after merging becomes a target value. The opening and / or opening time of the valve 83 is controlled. The salt concentration of the sherbet ice after merging can be adjusted only by controlling the opening degree and / or opening time of the proportional control valve 83 provided in the water flow path 80.
 また、前述した第1の実施形態では、供給路31と水流路80の合流部よりもシャーベット氷の流れ方向下流側に、シャーベット氷の温度を検出する温度センサ84が設けられており、検出された温度が目標値になるように制御装置25のCPU25aが比例制御弁83の開度及び/又は開時間を制御する。温度センサ84で検出された温度を用いて比例制御弁83を制御することで合流後のシャーベット氷の塩分濃度を調整することができる。この場合、シャーベット氷の塩分濃度と温度との間には相関関係が存在するので、温度センサ84により検出された温度からシャーベット氷の塩分濃度を演算することができる。 Further, in the first embodiment described above, the temperature sensor 84 for detecting the temperature of the sherbet ice is provided on the downstream side in the flow direction of the sherbet ice from the confluence of the supply path 31 and the water flow path 80, and is detected. The CPU 25a of the control device 25 controls the opening and / or opening time of the proportional control valve 83 so that the temperature becomes the target value. By controlling the proportional control valve 83 using the temperature detected by the temperature sensor 84, the salt concentration of the sherbet ice after merging can be adjusted. In this case, since there is a correlation between the salt concentration of sherbet ice and the temperature, the salt concentration of sherbet ice can be calculated from the temperature detected by the temperature sensor 84.
 また、前述した第1の実施形態では、貯氷タンクT内に温度センサ92が配設されており、この温度センサ92により検出される運転前の海水の温度及び運転開始後のシャーベット氷の温度に基づいて、制御装置25のCPU25aによって当該シャーベット氷の塩分濃度を演算している。そして、演算された塩分濃度に基づいて、水流路80から供給路31に合流させる水の流量を調整することでユーザに供給されるシャーベット氷の塩分濃度を調整することができる。 Further, in the first embodiment described above, the temperature sensor 92 is arranged in the ice storage tank T, and the temperature of the seawater before the operation and the temperature of the sherbet ice after the start of the operation are detected by the temperature sensor 92. Based on this, the CPU 25a of the control device 25 calculates the salt concentration of the sherbet ice. Then, the salt concentration of the sherbet ice supplied to the user can be adjusted by adjusting the flow rate of the water merging from the water flow path 80 to the supply path 31 based on the calculated salt concentration.
 また、前述した第1の実施形態では、温度センサ92でシャーベット氷の温度を検出することで、当該検出した温度から制御装置25のCPU25aで塩分濃度を演算している。そして、制御装置25のCPU25aは、演算された塩分濃度が所定範囲内でない場合、貯氷タンクT内のシャーベット氷の取出操作を禁止する。貯氷タンクT内のシャーベット氷の塩分濃度が低すぎる場合、当該シャーベット氷のIPFも低く、シャーベット氷としての利用が不十分である。検出された塩分濃度が所定範囲内でない場合に、貯氷タンク内のシャーベット氷の取出操作を禁止することで、ユーザに不十分な状態のシャーベット氷が供給されるのを抑制することができる。 Further, in the first embodiment described above, the temperature of the sherbet ice is detected by the temperature sensor 92, and the salt concentration is calculated by the CPU 25a of the control device 25 from the detected temperature. Then, the CPU 25a of the control device 25 prohibits the operation of taking out the sherbet ice in the ice storage tank T when the calculated salt concentration is not within the predetermined range. If the salt concentration of the sherbet ice in the ice storage tank T is too low, the IPF of the sherbet ice is also low, and the use as sherbet ice is insufficient. By prohibiting the operation of taking out the sherbet ice in the ice storage tank when the detected salt concentration is not within the predetermined range, it is possible to suppress the supply of the sherbet ice in an insufficient state to the user.
 また、前述した第1の実施形態では、制御装置25に通信可能に接続された入力部26が設けられており、ユーザは、貯氷タンクTから取り出すシャーベット氷の塩分濃度及び量を入力することで、所望の塩分濃度を有するシャーベット氷を所望の量だけ供給口39から取り出すことができる。 Further, in the first embodiment described above, the control device 25 is provided with an input unit 26 communicatively connected, and the user can input the salt concentration and amount of sherbet ice taken out from the ice storage tank T. , A desired amount of sherbet ice having a desired salt concentration can be taken out from the supply port 39.
 また、前述した第1の実施形態では、供給路31は、貯氷タンクT内のシャーベット氷を取り出す取出口42を有しており、この取出口42は、貯氷タンクT内のシャーベット氷の液面Lから所定距離だけ下方に配置されている。シャーベット氷を構成する微細氷は海水よりも比重が小さいことから浮力により上方に移動するので、貯氷タンクT内において液面付近のシャーベット氷は底面付近のシャーベット氷よりも高いIPFを有している。貯氷タンクT内のシャーベット氷の液面Lから所定距離だけ下方に配置されている取出口42により液面付近のシャーベット氷を取り出すことで、高IPFのシャーベット氷をユーザに供給することができる。 Further, in the first embodiment described above, the supply path 31 has an outlet 42 for taking out the sherbet ice in the ice storage tank T, and this outlet 42 is the liquid level of the sherbet ice in the ice storage tank T. It is arranged below by a predetermined distance from L. Since the fine ice that constitutes sherbet ice has a lower specific density than seawater, it moves upward due to buoyancy. Therefore, the sherbet ice near the liquid surface in the ice storage tank T has a higher IPF than the sherbet ice near the bottom surface. .. High IPF sherbet ice can be supplied to the user by taking out the sherbet ice near the liquid level through the outlet 42 arranged below the liquid level L of the sherbet ice in the ice storage tank T by a predetermined distance.
 また、前述した第1の実施形態(製氷システムの実施形態)では、貯氷タンクTからシャーベット氷を取り出す供給路31に、水が流れる水流路80が合流している。これにより、供給路31に合流させる水の流量を調整することでユーザに供給されるシャーベット氷の塩分濃度を容易に調整することができる。所定量のシャーベット氷をユーザに供給した後に、例えば、種類が異なる海水魚を保冷するためのシャーベット氷が必要になったときでも、供給路31に合流させる水流路80からの水の流量を調整するだけで容易にシャーベット氷の塩分濃度を調整することができるので、製氷システムSの使い勝手がよくなる。 Further, in the first embodiment described above (the embodiment of the ice making system), the water flow path 80 through which water flows joins the supply path 31 for taking out sherbet ice from the ice storage tank T. Thereby, the salt concentration of the sherbet ice supplied to the user can be easily adjusted by adjusting the flow rate of the water merging into the supply path 31. After supplying a predetermined amount of sherbet ice to the user, for example, even when sherbet ice for cooling different types of saltwater fish is needed, the flow rate of water from the water flow path 80 to be merged with the supply path 31 is adjusted. Since the salt concentration of sherbet ice can be easily adjusted just by doing so, the usability of the ice making system S is improved.
[第2の実施形態]
 図7は、本開示の第2の実施形態に係る製氷システムの説明図である。図8は、図7に示される製氷システムの制御装置の説明図である。
 本実施形態の製氷システムSは、第1の実施形態と同様に、製氷装置Iと氷供給装置Cとを備える。さらに、本実施形態の製氷システムSは、冷却装置100と温度センサ(第3温度センサ)103とを備えている。冷却装置100は、水流路80に流される水を冷却する。第3温度センサ103は、冷却装置100で冷却された水の温度を検出する。
[Second Embodiment]
FIG. 7 is an explanatory diagram of the ice making system according to the second embodiment of the present disclosure. FIG. 8 is an explanatory diagram of the control device of the ice making system shown in FIG.
The ice making system S of the present embodiment includes an ice making device I and an ice supply device C as in the first embodiment. Further, the ice making system S of the present embodiment includes a cooling device 100 and a temperature sensor (third temperature sensor) 103. The cooling device 100 cools the water flowing through the water flow path 80. The third temperature sensor 103 detects the temperature of the water cooled by the cooling device 100.
 本実施形態の冷却装置100及び第3温度センサ103は、氷供給装置Cの構成要素である水タンク81内に配置されている。冷却装置100は、熱交換器(第3熱交換器)により構成されている。以下、冷却装置100を構成する熱交換器を冷却用熱交換器100ともいう。冷却用熱交換器100は、水タンク81内に挿入され、水タンク81内の水と熱交換を行う。冷却用熱交換器100は、例えば、冷媒が流れる伝熱管をコイル状に巻いた構成を採用することができる。 The cooling device 100 and the third temperature sensor 103 of the present embodiment are arranged in the water tank 81 which is a component of the ice supply device C. The cooling device 100 is composed of a heat exchanger (third heat exchanger). Hereinafter, the heat exchanger constituting the cooling device 100 is also referred to as a cooling heat exchanger 100. The cooling heat exchanger 100 is inserted into the water tank 81 and exchanges heat with the water in the water tank 81. The cooling heat exchanger 100 can adopt, for example, a configuration in which a heat transfer tube through which a refrigerant flows is wound in a coil shape.
 本実施形態の冷却用熱交換器100には、製氷装置Iで用いられる冷媒が供給される。製氷装置Iは、第1の実施形態と同様に、利用側熱交換器(第2熱交換器)を構成する製氷機1、圧縮機2、熱源側熱交換器(第1熱交換器)3、四路切換弁4、利用側膨張弁5、熱源側膨張弁6、内部熱交換器7、及びレシーバ8を備えている。これらの機器は、冷媒配管96で接続されることによって冷媒回路95を構成している。 The cooling heat exchanger 100 of the present embodiment is supplied with the refrigerant used in the ice making device I. Similar to the first embodiment, the ice making device I includes an ice making machine 1, a compressor 2, and a heat source side heat exchanger (first heat exchanger) 3 that constitute a user-side heat exchanger (second heat exchanger). , A four-way switching valve 4, a utilization-side expansion valve 5, a heat source-side expansion valve 6, an internal heat exchanger 7, and a receiver 8. These devices form a refrigerant circuit 95 by being connected by a refrigerant pipe 96.
 熱源側熱交換器3における液冷媒の流出部3aと利用側膨張弁5との間の冷媒配管96a、より詳しくは、レシーバ8と内部熱交換器7との間の冷媒配管96aから、第1分岐管97が分岐している。製氷機1におけるガス冷媒の流出部1aと圧縮機2のガス冷媒の吸入部2aとの間の冷媒配管96b、より詳しくは、内部熱交換器7と四路切換弁4との間の冷媒配管96bから、第2分岐管98が分岐している。第1分岐管97は、冷却用熱交換器100の冷媒入口100aに接続されている。第2分岐管98は、冷却用熱交換器100の冷媒出口100bに接続されている。 From the refrigerant pipe 96a between the liquid refrigerant outflow portion 3a and the utilization side expansion valve 5 in the heat source side heat exchanger 3, more specifically, from the refrigerant pipe 96a between the receiver 8 and the internal heat exchanger 7, the first The branch pipe 97 is branched. Refrigerant pipe 96b between the outflow part 1a of the gas refrigerant in the ice maker 1 and the suction part 2a of the gas refrigerant of the compressor 2, more specifically, the refrigerant pipe between the internal heat exchanger 7 and the four-way switching valve 4. The second branch pipe 98 branches from 96b. The first branch pipe 97 is connected to the refrigerant inlet 100a of the cooling heat exchanger 100. The second branch pipe 98 is connected to the refrigerant outlet 100b of the cooling heat exchanger 100.
 熱源側熱交換器3で放熱された冷媒は、熱源側膨張弁6及びレシーバ8を通った後、冷媒配管96aから第1分岐管97へ分岐して冷却用熱交換器100に流入する。冷却用熱交換器100を通過した冷媒は、第2分岐管98を通って冷媒配管96bに合流し、四路切換弁4を通過して圧縮機2に吸入される。冷却用熱交換器100は、製氷機1と並列に冷媒回路95に設けられている。 The refrigerant radiated by the heat source side heat exchanger 3 passes through the heat source side expansion valve 6 and the receiver 8, then branches from the refrigerant pipe 96a to the first branch pipe 97 and flows into the cooling heat exchanger 100. The refrigerant that has passed through the cooling heat exchanger 100 joins the refrigerant pipe 96b through the second branch pipe 98, passes through the four-way switching valve 4, and is sucked into the compressor 2. The cooling heat exchanger 100 is provided in the refrigerant circuit 95 in parallel with the ice maker 1.
 第1分岐管97には、冷媒を減圧する冷却用膨張弁101が設けられている。第1分岐管97を流れる液冷媒は、冷却用膨張弁101において減圧され、低温低圧の気液二相冷媒となり、冷却用熱交換器100に供給される。冷却用熱交換器100では、水タンク81内の水と冷媒との間で熱交換が行われる。この熱交換で、冷媒は水タンク81内の水から吸熱して蒸発し、水タンク81内の水は冷却される。 The first branch pipe 97 is provided with a cooling expansion valve 101 for reducing the pressure of the refrigerant. The liquid refrigerant flowing through the first branch pipe 97 is depressurized by the cooling expansion valve 101 to become a low-temperature low-pressure gas-liquid two-phase refrigerant, which is supplied to the cooling heat exchanger 100. In the cooling heat exchanger 100, heat exchange is performed between the water in the water tank 81 and the refrigerant. By this heat exchange, the refrigerant absorbs heat from the water in the water tank 81 and evaporates, and the water in the water tank 81 is cooled.
 冷却用膨張弁101は、開くことによって冷却用熱交換器100に冷媒を供給し、閉じることによって冷却用熱交換器100への冷媒の供給を停止する。したがって、冷却用膨張弁101は、冷却用熱交換器100への冷媒の流れを制御する制御弁として機能する。冷却用膨張弁101は、第3温度センサ103の検出温度に基づいて開閉する。具体的に、第3温度センサ103で検出された温度が所定の上限温度Tth1を超えたとき、冷却用膨張弁101が開き、水タンク81内の水が冷却される。第3温度センサ103で検出された水の温度が所定の下限温度Tth2を下回ったとき、冷却用膨張弁101が閉じ、水タンク81内の水の冷却が停止する。上限温度Tth1は、供給路31で水と合流したシャーベット氷が過度に溶けない温度とすることができる。例えば、上限温度Tth1は、5℃とすることができる。下限温度Tth2は、水タンク81内の水が凍らない温度とすることができる。例えば、下限温度Tth2は、2℃とすることができる。水が凍らない温度に下限温度Tth2を設定することで、シャーベット氷と水との合流が不能となってしまうのを抑制することができる。 The cooling expansion valve 101 supplies the refrigerant to the cooling heat exchanger 100 by opening, and stops the supply of the refrigerant to the cooling heat exchanger 100 by closing. Therefore, the cooling expansion valve 101 functions as a control valve that controls the flow of the refrigerant to the cooling heat exchanger 100. The cooling expansion valve 101 opens and closes based on the temperature detected by the third temperature sensor 103. Specifically, when the temperature detected by the third temperature sensor 103 exceeds a predetermined upper limit temperature T th1 , the cooling expansion valve 101 opens and the water in the water tank 81 is cooled. When the temperature of the water detected by the third temperature sensor 103 falls below the predetermined lower limit temperature T th2 , the cooling expansion valve 101 closes and the cooling of the water in the water tank 81 stops. The upper limit temperature T th1 can be set to a temperature at which the sherbet ice that has merged with water in the supply path 31 does not excessively melt. For example, the upper limit temperature T th1 can be 5 ° C. The lower limit temperature T th2 can be set to a temperature at which the water in the water tank 81 does not freeze. For example, the lower limit temperature T th2 can be 2 ° C. By setting the lower limit temperature T th2 to a temperature at which water does not freeze, it is possible to suppress the inability to merge the sherbet ice and water.
 第3温度センサ103は、水タンク81の下部側(水タンク81の上下方向の中央よりも下側)に配置されている。そのため、水タンク81内の水の、より低い温度を検出することができる。第3温度センサ103は、好ましくは冷却用熱交換器100よりも下側に配置される。第3温度センサ103は、より好ましくは水タンク81の底面の近傍に配置される。 The third temperature sensor 103 is arranged on the lower side of the water tank 81 (below the center in the vertical direction of the water tank 81). Therefore, the lower temperature of the water in the water tank 81 can be detected. The third temperature sensor 103 is preferably arranged below the cooling heat exchanger 100. The third temperature sensor 103 is more preferably arranged near the bottom surface of the water tank 81.
 第2分岐管98には、第5温度センサ105が設けられている。第5温度センサ105は、冷却用熱交換器100を通過した後の冷媒の温度を検出する。冷却用膨張弁101が開いているとき、第5温度センサ105の検出結果を用いて求められた冷媒の過熱度が所定の設定値となるように、冷却用膨張弁101の開度が調整される。 The second branch pipe 98 is provided with a fifth temperature sensor 105. The fifth temperature sensor 105 detects the temperature of the refrigerant after passing through the cooling heat exchanger 100. When the cooling expansion valve 101 is open, the opening degree of the cooling expansion valve 101 is adjusted so that the degree of superheat of the refrigerant obtained using the detection result of the fifth temperature sensor 105 becomes a predetermined set value. To.
 冷却用膨張弁101は、製氷装置Iの制御部(第2制御部)27によって開閉動作が制御される。制御部27は、氷供給装置Cの制御装置25と同様に、CPU27aと、RAM、ROM等のメモリ27bと、外部の機器やセンサ等との受発信を行う受発信部27cとを備えている。制御部27は、メモリ27bに格納されたコンピュータプログラムをCPU27aが実行することにより、製氷装置Iの運転制御を含む、製氷システムSの運転に関する種々の制御を実現する。制御部27は、圧縮機2、四路切換弁4、膨張弁5,6,101等の駆動を制御する。制御部27は、第5温度センサ105等の検知信号を受発信部27cで受信する。制御部27は、氷供給装置Cの制御装置25と通信可能に接続されており、制御装置25が受信した温度センサ103、104等の検出結果を取得する。 The opening / closing operation of the cooling expansion valve 101 is controlled by the control unit (second control unit) 27 of the ice making device I. Like the control device 25 of the ice supply device C, the control unit 27 includes a CPU 27a, a memory 27b such as a RAM and a ROM, and a transmission / reception unit 27c that transmits / receives to / from an external device, a sensor, or the like. .. The control unit 27 realizes various controls related to the operation of the ice making system S, including the operation control of the ice making device I, by the CPU 27a executing the computer program stored in the memory 27b. The control unit 27 controls the drive of the compressor 2, the four-way switching valve 4, the expansion valves 5, 6, 101 and the like. The control unit 27 receives a detection signal from the fifth temperature sensor 105 or the like at the transmission / reception unit 27c. The control unit 27 is communicably connected to the control device 25 of the ice supply device C, and acquires the detection results of the temperature sensors 103, 104, etc. received by the control device 25.
 水流路80には、第4温度センサ104が設けられている。第4温度センサ104は、供給路31に合流する直前の水の温度を検出する。供給路31に合流する水の温度が高いと、合流後のシャーベット氷が溶けやすくなり、シャーベット氷の塩分濃度が低下するとともに温度が急速に上昇する可能性がある。そのため、第4温度センサ104によって合流前の水の温度が検出され、その検出結果に基づいて比例制御弁83の開度が調整される。比例制御弁83の開度の調整は、第1の実施形態と同様に、制御装置25によって行われる。 A fourth temperature sensor 104 is provided in the water flow path 80. The fourth temperature sensor 104 detects the temperature of water immediately before merging with the supply path 31. If the temperature of the water merging into the supply path 31 is high, the sherbet ice after merging tends to melt, and the salt concentration of the sherbet ice may decrease and the temperature may rise rapidly. Therefore, the temperature of the water before merging is detected by the fourth temperature sensor 104, and the opening degree of the proportional control valve 83 is adjusted based on the detection result. The opening degree of the proportional control valve 83 is adjusted by the control device 25 as in the first embodiment.
 (水タンク内の水温制御)
 図9は、水タンク内の水温制御の一例を示すフローチャートである。
 制御部27は、図9に示す手順により水タンク81内の水を冷却し、水温を所定の範囲内に維持する。制御部27は、まず、水タンク81内の第3温度センサ103から検知信号を受信することによって、水温Tを取得する(ステップS11)。
(Water temperature control in the water tank)
FIG. 9 is a flowchart showing an example of water temperature control in the water tank.
The control unit 27 cools the water in the water tank 81 according to the procedure shown in FIG. 9 and maintains the water temperature within a predetermined range. First, the control unit 27 acquires the water temperature T by receiving a detection signal from the third temperature sensor 103 in the water tank 81 (step S11).
 次いで、制御部27は、水温Tが所定の上限温度Tth1を超えているか否かを判断する(ステップS12)。この上限温度Tth1は、上述したように5℃とすることができる。制御部27は、ステップS12における判断が肯定的(YES)である場合、水タンク81の水を冷却するために冷却用膨張弁101を開く制御を実行する(ステップS13)。 Next, the control unit 27 determines whether or not the water temperature T exceeds a predetermined upper limit temperature T th1 (step S12). The upper limit temperature T th1 can be 5 ° C. as described above. When the determination in step S12 is affirmative (YES), the control unit 27 executes control to open the cooling expansion valve 101 to cool the water in the water tank 81 (step S13).
 制御部27は、ステップS12における判断が否定的(NO)である場合、さらに、水温Tが所定の下限温度Tth2を下回っているか否かを判断する(ステップS14)。この下限温度Tth2は、上述したように2℃とすることができる。制御部27は、ステップS14における判断が肯定的(YES)である場合、冷却用膨張弁101を閉じる制御を行う(ステップS15)。具体的に、制御部27は、冷却用膨張弁101が開いている場合には当該冷却用膨張弁101を閉じ、冷却用膨張弁101が閉じている場合には閉じた状態を維持する。これによって、水タンク81内の水の冷却が停止した状態となる。 When the determination in step S12 is negative (NO), the control unit 27 further determines whether or not the water temperature T is below the predetermined lower limit temperature T th2 (step S14). The lower limit temperature T th2 can be 2 ° C. as described above. When the determination in step S14 is positive (YES), the control unit 27 controls to close the cooling expansion valve 101 (step S15). Specifically, the control unit 27 closes the cooling expansion valve 101 when the cooling expansion valve 101 is open, and maintains the closed state when the cooling expansion valve 101 is closed. As a result, the cooling of the water in the water tank 81 is stopped.
 制御部27は、ステップS14における判断が否定的(NO)である場合、冷却用膨張弁101の開閉状態を維持する(ステップS16)。具体的に、制御部27は、冷却用膨張弁101が開いている場合には、開いた状態を維持し、冷却用膨張弁101が閉じている場合には、閉じた状態を維持する。 When the judgment in step S14 is negative (NO), the control unit 27 maintains the open / closed state of the cooling expansion valve 101 (step S16). Specifically, the control unit 27 maintains an open state when the cooling expansion valve 101 is open, and maintains a closed state when the cooling expansion valve 101 is closed.
 制御部27は、以上の手順を繰り返し行うことによって、水タンク81内の水の温度を所定の範囲Tth1~Tth2内に維持することができる。 By repeating the above procedure, the control unit 27 can maintain the temperature of the water in the water tank 81 within a predetermined range T th1 to T th2.
 (比例制御弁の制御)
 本実施形態の制御装置25は、水流路80を流れる水の温度に応じて比例制御弁83の開度を調整する。具体的に、制御装置25は、貯氷タンクT内のシャーベット氷の温度(塩分濃度)と、ユーザが取り出したいシャーベット氷の温度(塩分濃度)と、シャーベット氷に合流させる水の温度とから、貯氷タンクTのシャーベット氷に合流させる水の量を求め、比例制御弁83の開度を調整する。
(Control of proportional control valve)
The control device 25 of the present embodiment adjusts the opening degree of the proportional control valve 83 according to the temperature of the water flowing through the water flow path 80. Specifically, the control device 25 stores ice based on the temperature (salt concentration) of the sherbet ice in the ice storage tank T, the temperature of the sherbet ice (salt concentration) that the user wants to take out, and the temperature of the water to be merged with the sherbet ice. The amount of water to be merged with the sherbet ice in the tank T is obtained, and the opening degree of the proportional control valve 83 is adjusted.
 例えば、貯氷タンクT内のシャーベット氷が-3℃であり、設定温度として-1.5℃のシャーベット氷を取り出すとき、制御装置25は、水流路80を流れる水の温度が2℃である場合と5℃である場合とで比例制御弁83の開度を異ならせる。具体的に、制御装置25は、水の温度が5℃である場合には、2℃である場合よりも比例制御弁83の開度を小さくする。 For example, when the sherbet ice in the ice storage tank T is -3 ° C and the sherbet ice having a set temperature of −1.5 ° C is taken out, the control device 25 determines that the temperature of the water flowing through the water flow path 80 is 2 ° C. The opening degree of the proportional control valve 83 is different between the case where the temperature is 5 ° C. Specifically, the control device 25 makes the opening degree of the proportional control valve 83 smaller when the water temperature is 5 ° C. than when the water temperature is 2 ° C.
 仮に、水の温度が2℃である場合と5℃である場合とで比例制御弁83の開度を同じにしたとすると、5℃の水を合流させた場合の方が2℃の水を合流させる場合よりも、シャーベット氷のIPFが大きく変化し、より早く設定温度に達する。そのため、シャーベット氷の温度が設定温度を超えてしまう可能性も高くなる。 Assuming that the opening degree of the proportional control valve 83 is the same when the temperature of the water is 2 ° C. and when the temperature is 5 ° C., the water at 2 ° C. is produced when the water at 5 ° C. is merged. The IPF of sherbet ice changes significantly and reaches the set temperature earlier than when merging. Therefore, there is a high possibility that the temperature of sherbet ice will exceed the set temperature.
 本実施形態の制御装置25は、水の温度が5℃である場合には、2℃である場合よりも比例制御弁83の開度を小さくすることによって、IPFの変化を小さくし、設定温度に達する時間を長くしている。これにより、シャーベット氷の温度が設定温度を超えてしまうのを抑制することができる。 The control device 25 of the present embodiment reduces the change in IPF by making the opening degree of the proportional control valve 83 smaller when the water temperature is 5 ° C. than when the water temperature is 2 ° C., and the set temperature. It takes longer to reach. As a result, it is possible to prevent the temperature of the sherbet ice from exceeding the set temperature.
 本実施形態では、水タンク81内の水温が2℃~5℃に制御されているので、制御装置25は、最も低い2℃を「基準温度」とし、このときの比例制御弁83の開度を「基準開度」とする。制御装置25は、水温が基準温度を超えた場合には、比例制御弁83の開度を基準開度から閉じる方向に操作する。また、制御装置25は、基準温度を超えた水の温度が高くなるほど、比例制御弁93の開度を閉じる方向へ大きく操作するように構成されている。 In the present embodiment, since the water temperature in the water tank 81 is controlled to 2 ° C. to 5 ° C., the control device 25 sets the lowest 2 ° C. as the "reference temperature" and sets the opening degree of the proportional control valve 83 at this time. Is the "reference opening". When the water temperature exceeds the reference temperature, the control device 25 operates the opening degree of the proportional control valve 83 in the direction of closing from the reference opening degree. Further, the control device 25 is configured to operate the proportional control valve 93 more in the closing direction as the temperature of the water exceeding the reference temperature becomes higher.
 図10は、比例制御弁の制御の一例を示すフローチャートである。
 制御装置25は、図10に示す手順により比例制御弁の開度を制御し、シャーベット氷の温度を設定温度に調整する。まず、制御装置25は、水流路80に設けられた第4温度センサ104から検知信号を受信することによって、水温を取得する(ステップS21)。
FIG. 10 is a flowchart showing an example of control of the proportional control valve.
The control device 25 controls the opening degree of the proportional control valve according to the procedure shown in FIG. 10 and adjusts the temperature of the sherbet ice to the set temperature. First, the control device 25 acquires the water temperature by receiving a detection signal from the fourth temperature sensor 104 provided in the water flow path 80 (step S21).
 次いで、制御装置25は、水温と基準温度(例えば2℃)との差分を算出する(ステップS22)。そして、制御装置25は、この差分を用いて基準開度からの比例制御弁83の操作量(閉じる量)を算出する(ステップS23)。
 次いで、制御装置25は、算出した操作量に応じて比例制御弁83を操作し、水流路80から供給路31へ水を合流させる(ステップS24)。
Next, the control device 25 calculates the difference between the water temperature and the reference temperature (for example, 2 ° C.) (step S22). Then, the control device 25 calculates the operation amount (close amount) of the proportional control valve 83 from the reference opening degree by using this difference (step S23).
Next, the control device 25 operates the proportional control valve 83 according to the calculated operation amount to merge water from the water flow path 80 into the supply path 31 (step S24).
 [第2の実施形態の作用効果]
 第2の実施形態の氷供給装置C及び製氷システムSは、第1の実施形態の作用効果に加えて、次の作用効果を奏する。
 前述した第2の実施形態の氷供給装置Cでは、水流路80には、冷却された水が流れる。そのため、合流した水によってシャーベット氷が溶けるのを抑制し、高IPFのシャーベット氷をユーザに供給することができる。
[Action and effect of the second embodiment]
The ice supply device C and the ice making system S of the second embodiment have the following effects in addition to the effects of the first embodiment.
In the ice supply device C of the second embodiment described above, cooled water flows through the water flow path 80. Therefore, it is possible to suppress the melting of sherbet ice by the merged water and supply the high IPF sherbet ice to the user.
 前述した第2の実施形態では、氷供給装置Cが、水流路80に流される水を冷却する冷却装置100を備えている。したがって、合流した水によってシャーベット氷が溶けるのを抑制し、高IPFのシャーベット氷をユーザに供給することができる。 In the second embodiment described above, the ice supply device C includes a cooling device 100 that cools the water flowing through the water flow path 80. Therefore, it is possible to suppress the melting of sherbet ice by the merged water and supply the user with high IPF sherbet ice.
 前述した第2の実施形態の製氷システムSは、シャーベット氷を生成する冷媒回路95と、氷供給装置Cとを備える。そのため、冷媒回路95で生成したシャーベット氷を貯氷タンクTに貯留し、貯氷タンクTからシャーベット氷を取り出す供給路31に水を合流させることができる。これにより、ユーザに供給されるシャーベット氷の塩分濃度を調整することができる。 The ice making system S of the second embodiment described above includes a refrigerant circuit 95 for generating sherbet ice and an ice supply device C. Therefore, the sherbet ice generated by the refrigerant circuit 95 can be stored in the ice storage tank T, and water can be merged with the supply path 31 for taking out the sherbet ice from the ice storage tank T. This makes it possible to adjust the salt concentration of the sherbet ice supplied to the user.
 前述した第2の実施形態では、冷媒回路95が、圧縮機2と、圧縮機2で圧縮された冷媒を放熱する熱源側熱交換器(第1熱交換器)3と、熱源側熱交換器3で放熱された冷媒とシャーベット氷の原料となる被冷却媒体とを熱交換し当該被冷却媒体を冷却する利用側熱交換器(第2熱交換器)である製氷機1とを含む。そのため、冷媒回路95を流れる冷媒により被冷却媒体を冷却してシャーベット氷を生成することができる。 In the second embodiment described above, the refrigerant circuit 95 includes a compressor 2, a heat source side heat exchanger (first heat exchanger) 3 that dissipates heat from the refrigerant compressed by the compressor 2, and a heat source side heat exchanger. It includes an ice maker 1 which is a user-side heat exchanger (second heat exchanger) that exchanges heat between the refrigerant radiated in 3 and the cooled medium used as a raw material for sherbet ice to cool the cooled medium. Therefore, the cooling medium can be cooled by the refrigerant flowing through the refrigerant circuit 95 to generate sherbet ice.
 前述した第2の実施形態では、冷媒回路95が、熱源側熱交換器3で放熱された冷媒と水流路80に流される水とを熱交換し当該水を冷却する冷却用熱交換器(第3熱交換器)100をさらに含む。そのため、シャーベット氷を生成する冷媒回路95の冷媒を利用して水流路80に流される水を冷却することができる。 In the second embodiment described above, the refrigerant circuit 95 exchanges heat between the refrigerant dissipated by the heat source side heat exchanger 3 and the water flowing through the water flow path 80 to cool the water (first). 3 Heat exchanger) 100 is further included. Therefore, the water flowing through the water flow path 80 can be cooled by using the refrigerant of the refrigerant circuit 95 that generates sherbet ice.
 前述した第2の実施形態では、冷却用熱交換器100によって冷却される水を貯留する水タンク81をさらに備える。そのため、供給路31に対して冷却された水を安定して供給することができる。 In the second embodiment described above, a water tank 81 for storing water cooled by the cooling heat exchanger 100 is further provided. Therefore, the cooled water can be stably supplied to the supply path 31.
 前述した第2の実施形態では、水タンク81内の水の温度を検出する第3温度センサ103と、冷却用熱交換器100における冷媒の流れを制御する冷却用膨張弁(制御弁)101と、第3温度センサ103の検出温度に基づいて、冷却用膨張弁101の動作を制御する制御部(第2制御部)27と、を備える。そのため、水タンク81内の水の温度を適切に制御することができる。 In the second embodiment described above, the third temperature sensor 103 that detects the temperature of the water in the water tank 81, and the cooling expansion valve (control valve) 101 that controls the flow of the refrigerant in the cooling heat exchanger 100. A control unit (second control unit) 27 that controls the operation of the cooling expansion valve 101 based on the detection temperature of the third temperature sensor 103 is provided. Therefore, the temperature of the water in the water tank 81 can be appropriately controlled.
 前述した第2の実施形態では、第3温度センサ103が、水タンク81内の下部側に配置される。そのため、水タンク81内に貯留された水のなかで、できるだけ低い温度を検出することができ、この温度に基づいて冷却用膨張弁101の動作を制御することで、水タンク81内の水が必要以上に冷却される(凍る)のを抑制することができる。 In the second embodiment described above, the third temperature sensor 103 is arranged on the lower side in the water tank 81. Therefore, it is possible to detect the lowest possible temperature in the water stored in the water tank 81, and by controlling the operation of the cooling expansion valve 101 based on this temperature, the water in the water tank 81 can be detected. It is possible to suppress cooling (freezing) more than necessary.
[その他の変形例]
 本開示は前述した実施形態に限定されるものではなく、特許請求の範囲内において種々の変更が可能である。
 例えば、前述した実施形態では、貯氷タンクは、水平断面が矩形の角筒形状を呈しているが、本開示はこれに限定されない。貯氷タンクは、水平断面が円形の円筒形状を呈するタンクとしてもよいし、水平断面が多角形状を呈するタンクとしてもよい。
[Other variants]
The present disclosure is not limited to the above-described embodiment, and various modifications can be made within the scope of the claims.
For example, in the above-described embodiment, the ice storage tank has a rectangular tube shape having a rectangular horizontal cross section, but the present disclosure is not limited to this. The ice storage tank may be a tank having a cylindrical shape with a circular horizontal cross section, or a tank having a polygonal shape with a horizontal cross section.
 また、前述した実施形態の蒸発器の代わりに、例えば、内管と外管との間の環状スペース内にノズルで冷媒を噴出するタイプの蒸発器を用いることもできる。 Further, instead of the evaporator of the above-described embodiment, for example, a type of evaporator that ejects the refrigerant with a nozzle in the annular space between the inner pipe and the outer pipe can be used.
 また、前述した実施形態では、製氷機として、内管及び外管の各軸が水平になるように配置された横置き型の二重管式製製氷機を例示したが、製氷機の構成は本開示において特に限定されるものではなく、内管及び外管の各軸が垂直になるように配置された縦置き型の二重管式製製氷機等、種々の形状及び構造の製氷機を採用することができる。 Further, in the above-described embodiment, as the ice maker, a horizontal double-tube ice maker in which the inner pipe and the outer pipe are arranged so that the axes are horizontal has been exemplified. The present disclosure is not particularly limited to ice makers having various shapes and structures, such as a vertical double-tube ice maker in which the axes of the inner tube and the outer tube are arranged to be vertical. Can be adopted.
 また、前述した実施形態では、入力部26に入力された、ユーザに供給されるシャーベット氷の塩分濃度及び量の調整について例示されていないが、例えば、第1温度センサ84により検知される値が目標塩分濃度に対応した温度になるように比例制御弁83の開度を制御することで当該シャーベット氷の塩分濃度を調整することができる。また、電磁弁37の近傍に流量を測定することができるセンサ(図示せず)を設け、目標とする量のシャーベット氷が供給されるまでの時間、当該電磁弁37を開放することでシャーベット氷の供給量を調整することができる。 Further, in the above-described embodiment, the adjustment of the salt concentration and the amount of sherbet ice supplied to the user, which is input to the input unit 26, is not exemplified, but for example, the value detected by the first temperature sensor 84 is used. The salt concentration of the sherbet ice can be adjusted by controlling the opening degree of the proportional control valve 83 so that the temperature corresponds to the target salt concentration. In addition, a sensor (not shown) capable of measuring the flow rate is provided in the vicinity of the solenoid valve 37, and the sherbet ice is opened by opening the solenoid valve 37 until the target amount of sherbet ice is supplied. Supply amount can be adjusted.
 前述した第2の実施形態において、冷却装置としての冷却用熱交換器は、水タンク外に配置されていてもよい。この場合、ポンプによって水タンクから水を引き出して循環させる水回路を設け、この水回路に冷却用熱交換器を設けることができる。 In the second embodiment described above, the cooling heat exchanger as the cooling device may be arranged outside the water tank. In this case, a water circuit that draws water from the water tank by a pump and circulates it can be provided, and a cooling heat exchanger can be provided in this water circuit.
 前述した第2の実施形態において、冷却装置としての冷却用熱交換器は、製氷装置の冷媒回路とは別の冷媒回路に設けられていてもよい。冷却装置は、冷媒を用いないものであってもよい。 In the second embodiment described above, the cooling heat exchanger as the cooling device may be provided in a refrigerant circuit different from the refrigerant circuit of the ice making device. The cooling device may not use a refrigerant.
 前述した第2の実施形態においては、比例制御弁の制御のために水流路に設けられた温度センサで水温を検出していたが、水タンク内の温度センサで水温を検出してもよい。ただし、水流路に設けられた温度センサによって、供給路に合流する直前の水温を検出することで、より正確な比例制御弁の制御を行うことができる。 In the second embodiment described above, the water temperature was detected by the temperature sensor provided in the water flow path for controlling the proportional control valve, but the water temperature may be detected by the temperature sensor in the water tank. However, the proportional control valve can be controlled more accurately by detecting the water temperature immediately before merging into the supply path by the temperature sensor provided in the water flow path.
 前述した第2の実施形態において、比例制御弁の制御は、水と合流した後のシャーベット氷の温度又は塩分濃度に基づいたフィードバック制御であってもよい。 In the second embodiment described above, the control of the proportional control valve may be feedback control based on the temperature or salinity of the sherbet ice after merging with water.
 前述した第2の実施形態において、水タンク内には、下部側だけでなく上部側にも温度センサを設けてもよい。
 前述した第2の実施形態において、水タンク内の水の温度範囲である2℃~5℃は例示であり、これとは異なる温度範囲であってもよい。
In the second embodiment described above, the temperature sensor may be provided not only on the lower side but also on the upper side in the water tank.
In the second embodiment described above, the temperature range of water in the water tank, 2 ° C. to 5 ° C., is an example, and the temperature range may be different from this.
 1 : 製氷機(第2熱交換器)
 2 : 圧縮機
 3 : 熱源側熱交換器(第1熱交換器)
 4 : 四路切換弁
 5 : 利用側膨張弁
 6 : 熱源側膨張弁
 7 : 内部熱交換器
 8 : レシーバ
10 : 送風ファン
11 : 内管
12 : 外管
13 : 蒸発器
14 : 氷掻き取り部
15 : 海水配管
16 : シャーベット配管
17 : 冷媒入口管
18 : 冷媒出口管
19 : 回転軸
20 : 支持バー
21 : ブレード
22 : モータ
23 : フランジ
24 : 環状スペース
25 : 制御装置
26 : 入力部
27 : 制御部
30 : 内壁
31 : 供給路
32 : ポンプ
33 : 水位センサ
34 : ホース
34a: 先端部
34b: 蛇腹部
35 : 配管
36 : チェーン
37 : 電磁弁
38 : ポンプ
40 : フロート
40a: 上面
40b: 底面
41 : 開口
42 : 取出口
50 : 還流路
51 : 安全弁
60 : 枝管
61 : 放出管
62 : 放出口
70 : 海水補給管
72 : 殺菌・ろ過装置
73 : 電磁弁
80 : 水流路
81 : 水タンク
83 : 比例制御弁
84 : 第1温度(濃度)センサ
86 : 制御弁
87 : フロートスイッチ
90 : 排出路
91 : 電磁弁
92 : 第2温度(濃度)センサ
95 : 冷媒回路
96 : 冷媒配管
97 : 第1分岐管
98 : 第2分岐管
100: 冷却用熱交換器(第3熱交換器、冷却装置)
101: 冷却用膨張弁(制御弁)
103: 第3温度センサ
104: 第4温度センサ
105: 第5温度センサ
 C : 氷供給装置
 I : 製氷装置
 L : 液面
 S : 製氷システム
 T : 貯氷タンク
 
1: Ice maker (second heat exchanger)
2: Compressor 3: Heat source side heat exchanger (first heat exchanger)
4: Four-way switching valve 5: Utilization side expansion valve 6: Heat source side expansion valve 7: Internal heat exchanger 8: Receiver 10: Blower fan 11: Inner pipe 12: Outer pipe 13: Evaporator 14: Ice scraper 15 : Seawater pipe 16: Sherbet pipe 17: Refrigerator inlet pipe 18: Refrigerator outlet pipe 19: Rotating shaft 20: Support bar 21: Blade 22: Motor 23: Flange 24: Ring space 25: Control device 26: Input unit 27: Control unit 30: Inner wall 31: Supply path 32: Pump 33: Water level sensor 34: Hose 34a: Tip 34b: Bellows 35: Piping 36: Chain 37: Electromagnetic valve 38: Pump 40: Float 40a: Top surface 40b: Bottom surface 41: Opening 42: Outlet 50: Recirculation path 51: Safety valve 60: Branch pipe 61: Discharge pipe 62: Discharge port 70: Seawater supply pipe 72: Sterilization / filtration device 73: Electromagnetic valve 80: Water flow path 81: Water tank 83: Proportional control Valve 84: First temperature (concentration) sensor 86: Control valve 87: Float switch 90: Discharge path 91: Electromagnetic valve 92: Second temperature (concentration) sensor 95: Refrigerator circuit 96: Refrigerator pipe 97: First branch pipe 98 : 2nd branch pipe 100: Cooling heat exchanger (3rd heat exchanger, cooling device)
101: Cooling expansion valve (control valve)
103: 3rd temperature sensor 104: 4th temperature sensor 105: 5th temperature sensor C: Ice supply device I: Ice making device L: Liquid level S: Ice making system T: Ice storage tank

Claims (19)

  1.  シャーベット氷を貯留する貯氷タンク(T)と、前記貯氷タンク(T)からシャーベット氷を取り出す供給路(31)と、前記供給路(31)に合流する、水が流れる水流路(80)と、を備えた氷供給装置(C)。 An ice storage tank (T) for storing sherbet ice, a supply path (31) for taking out sherbet ice from the ice storage tank (T), a water channel (80) through which water flows, which joins the supply path (31). An ice supply device (C) equipped with.
  2.  前記水流路(80)が前記供給路(31)に合流する合流部よりも、シャーベット氷の流れ方向下流側に配設されるポンプ(38)を更に備えた、請求項1に記載の氷供給装置(C)。 The ice supply according to claim 1, further comprising a pump (38) arranged on the downstream side in the flow direction of sherbet ice from the confluence portion where the water flow path (80) joins the supply path (31). Device (C).
  3.  前記水流路(80)に設けられた流量調整弁(83)と、合流後のシャーベット氷の塩分濃度が目標値となるように前記流量調整弁(83)を制御する制御部(25)とを更に備えた、請求項1又は請求項2に記載された氷供給装置(C)。 A flow rate adjusting valve (83) provided in the water flow path (80) and a control unit (25) for controlling the flow rate adjusting valve (83) so that the salt concentration of the sherbet ice after merging becomes a target value. The ice supply device (C) according to claim 1 or 2, further provided.
  4.  前記合流部よりもシャーベット氷の流れ方向下流側に、シャーベット氷の温度を検出する第1温度センサ(84)又は当該シャーベット氷の塩分濃度を検出する第1濃度センサ(84)を更に備え、
     前記制御部(25)は、前記第1温度センサ(84)により検出された温度又は前記第1濃度センサ(84)により検出された濃度が目標値になるように前記流量調整弁(83)を制御する、請求項3に記載の氷供給装置(C)。
    A first temperature sensor (84) for detecting the temperature of the sherbet ice or a first concentration sensor (84) for detecting the salt concentration of the sherbet ice is further provided downstream of the confluence in the flow direction of the sherbet ice.
    The control unit (25) adjusts the flow rate adjusting valve (83) so that the temperature detected by the first temperature sensor (84) or the concentration detected by the first concentration sensor (84) becomes a target value. The ice supply device (C) according to claim 3, which is controlled.
  5.  前記合流部よりもシャーベット氷の流れ方向下流側に、シャーベット氷の温度を検出する第1温度センサ(84)を更に備え、
     前記制御部(25)は、前記第1温度センサ(84)により検出された温度から塩分濃度を演算し、演算された前記塩分濃度が目標値となるように前記流量調整弁(83)を制御する、請求項3に記載の氷供給装置(C)。
    A first temperature sensor (84) for detecting the temperature of the sherbet ice is further provided downstream of the confluence in the flow direction of the sherbet ice.
    The control unit (25) calculates a salt concentration from the temperature detected by the first temperature sensor (84), and controls the flow rate adjusting valve (83) so that the calculated salt concentration becomes a target value. The ice supply device (C) according to claim 3.
  6.  前記制御部(25)は、前記流量調整弁(83)の開度及び/又は開時間を制御する、請求項3から請求項5のいずれか一項に記載の氷供給装置(C)。 The ice supply device (C) according to any one of claims 3 to 5, wherein the control unit (25) controls the opening degree and / or opening time of the flow rate adjusting valve (83).
  7.  前記貯氷タンク(T)内のシャーベット氷の塩分濃度を検出する第2濃度センサ(92)を更に備え、
     前記制御部(25)は、前記第2濃度センサ(92)により検出された塩分濃度が所定範囲内でない場合、前記貯氷タンク(T)内のシャーベット氷の取出操作を禁止する、請求項3から請求項6のいずれか一項に記載の氷供給装置(C)。
    A second concentration sensor (92) for detecting the salt concentration of sherbet ice in the ice storage tank (T) is further provided.
    The control unit (25) prohibits the operation of taking out the sherbet ice in the ice storage tank (T) when the salt concentration detected by the second concentration sensor (92) is not within the predetermined range, according to claim 3. The ice supply device (C) according to any one of claims 6.
  8.  前記貯氷タンク(T)内のシャーベット氷の温度を検出する第2温度センサ(92)と、
     製氷装置の運転前に前記貯氷タンク(T)に供給され前記第2温度センサ(92)により検出された被冷却媒体の温度と、製氷装置(I)の運転開始後に前記貯氷タンク(T)内に貯留され前記第2温度センサ(92)により検出されたシャーベット氷の温度とに基づいて当該シャーベット氷の塩分濃度を演算する塩分濃度演算部(25a)と
     を更に備えた、請求項1から請求項7のいずれか一項に記載の氷供給装置(C)。
    A second temperature sensor (92) that detects the temperature of sherbet ice in the ice storage tank (T), and
    The temperature of the medium to be cooled, which is supplied to the ice storage tank (T) before the operation of the ice making device (T) and detected by the second temperature sensor (92), and the inside of the ice storage tank (T) after the operation of the ice making device (I) is started. The claim 1 is further provided with a salt concentration calculation unit (25a) for calculating the salt concentration of the sherbet ice based on the temperature of the sherbet ice stored in the second temperature sensor (92) and detected by the second temperature sensor (92). Item 6. The ice supply device (C) according to any one of items 7.
  9.  前記貯氷タンク(T)から取り出すシャーベット氷の塩分濃度及び量を受け付ける入力部(26)を更に備えた、請求項1から請求項8のいずれか一項に記載の氷供給装置(C)。 The ice supply device (C) according to any one of claims 1 to 8, further comprising an input unit (26) for receiving the salt concentration and amount of sherbet ice taken out from the ice storage tank (T).
  10.  前記供給路(31)は、前記貯氷タンク(T)内に配設され、当該貯氷タンク(T)内のシャーベット氷を取り出す取出口(42)を有し、
     前記取出口(42)は、前記貯氷タンク(T)内のシャーベット氷の液面(L)から所定距離だけ下方に配置されている、請求項1から請求項9のいずれか一項に記載の氷供給装置(C)。
    The supply channel (31) is arranged in the ice storage tank (T) and has an outlet (42) for taking out sherbet ice in the ice storage tank (T).
    The outlet (42) is arranged below the liquid level (L) of sherbet ice in the ice storage tank (T) by a predetermined distance, according to any one of claims 1 to 9. Ice supply device (C).
  11.  前記水流路(80)には、冷却された水が流れる、請求項1から請求項10のいずれか一項に記載の氷供給装置(C)。 The ice supply device (C) according to any one of claims 1 to 10, wherein cooled water flows through the water flow path (80).
  12.  前記水流路(80)に流される水を冷却する冷却装置(100)を備える、請求項11に記載の氷供給装置(C)。 The ice supply device (C) according to claim 11, further comprising a cooling device (100) for cooling the water flowing through the water flow path (80).
  13.  前記シャーベット氷を生成する冷媒回路と、
     請求項1から請求項12のいずれか一項に記載の氷供給装置(C)とを備える、製氷システム(S)。
    The refrigerant circuit that produces the sherbet ice and
    An ice making system (S) comprising the ice supply device (C) according to any one of claims 1 to 12.
  14.  前記冷媒回路が、
      圧縮機(2)と、
      前記圧縮機(2)で圧縮された冷媒を放熱する第1熱交換器(3)と、
      前記第1熱交換器(3)で放熱された冷媒と前記シャーベット氷の原料となる被冷却媒体とを熱交換し当該被冷却媒体を冷却する第2熱交換器(1)と、を含む、請求項13に記載の製氷システム(S)。
    The refrigerant circuit
    Compressor (2) and
    The first heat exchanger (3) that dissipates heat from the refrigerant compressed by the compressor (2), and
    It includes a second heat exchanger (1) that cools the cooled medium by exchanging heat between the refrigerant radiated by the first heat exchanger (3) and the cooled medium that is the raw material of the sherbet ice. The ice making system (S) according to claim 13.
  15.  前記冷媒回路が、
      前記第1熱交換器(3)で放熱された冷媒と前記水流路(80)に流される水とを熱交換し当該水を冷却する第3熱交換器(100)をさらに含む、請求項14に記載の製氷システム(S)。
    The refrigerant circuit
    14. Claim 14 further includes a third heat exchanger (100) that cools the water by exchanging heat between the refrigerant radiated by the first heat exchanger (3) and the water flowing through the water flow path (80). The ice making system (S) according to.
  16.  前記第3熱交換器(100)によって冷却される水を貯留する水タンク(81)をさらに備える、請求項15に記載の製氷システム(S)。 The ice making system (S) according to claim 15, further comprising a water tank (81) for storing water cooled by the third heat exchanger (100).
  17.  前記水タンク(81)内の水の温度を検出する第3温度センサ(103)と、
     前記第3熱交換器(100)における冷媒の流れを制御する制御弁(101)と、
     前記第3温度センサ(103)の検出温度に基づいて、前記制御弁(101)の動作を制御する第2制御部(27)と、を備える、請求項16に記載の製氷システム(S)。
    A third temperature sensor (103) that detects the temperature of the water in the water tank (81), and
    A control valve (101) that controls the flow of the refrigerant in the third heat exchanger (100),
    The ice making system (S) according to claim 16, further comprising a second control unit (27) that controls the operation of the control valve (101) based on the detection temperature of the third temperature sensor (103).
  18.  前記第3温度センサ(103)が、前記水タンク(81)内の下部側に配置される、請求項17に記載の製氷システム(S)。 The ice making system (S) according to claim 17, wherein the third temperature sensor (103) is arranged on the lower side in the water tank (81).
  19.  製氷装置(I)と、
     請求項1から請求項12のいずれかの一項に記載の氷供給装置(C)と
     を備えた、製氷システム(S)。
     
    Ice making device (I) and
    An ice making system (S) comprising the ice supply device (C) according to any one of claims 1 to 12.
PCT/JP2020/048749 2019-12-27 2020-12-25 Ice supply device and ice making system WO2021132570A1 (en)

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