CN205460044U - Rubbish continuous sterilization device and system of trash disposal - Google Patents
Rubbish continuous sterilization device and system of trash disposal Download PDFInfo
- Publication number
- CN205460044U CN205460044U CN201620098944.1U CN201620098944U CN205460044U CN 205460044 U CN205460044 U CN 205460044U CN 201620098944 U CN201620098944 U CN 201620098944U CN 205460044 U CN205460044 U CN 205460044U
- Authority
- CN
- China
- Prior art keywords
- rubbish
- medium ball
- conveying
- conveying pipeline
- refuse
- Prior art date
- Legal status (The legal status 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 status listed.)
- Withdrawn - After Issue
Links
Landscapes
- Processing Of Solid Wastes (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
The utility model provides a rubbish continuous sterilization device still provides system of trash disposal. Rubbish continuous sterilization device, including rubbish temporary storage bin, solid pump, conveying pipeline, medium ball and heat exchanger, rubbish temporary storage bin's export and the entry of solid pump intercommunication, the entry and the solid delivery side of pump intercommunication of conveying pipeline, medium ball are used for mixing and carrying along the conveying pipeline with rubbish, and the heat exchanger is used for heating the conveying pipeline and gives rubbish and medium ball in the conveying pipeline through the conveying pipeline with heat transfer. The utility model discloses a sterilization is accomplished to this kind of rubbish continuous sterilization device in the conveying pipeline, also be promptly to sterilize under sealed environment, and non -staining environment, more importantly can carry out continuous sterilization, and sterilization efficiency is high moreover.
Description
Technical field
This utility model relates to technical field of waste treatment, in particular to a kind of rubbish continuous sterilizer and refuse disposal system.
Background technology
Medical waste Biocidal treatment method has two big class, i.e. burning method and non-burning methods at present.Burning method (comprises pyrolysismethod), and non-burning method includes high-temperature steam method, microwave sterilizating method, chemical disinfection and sterilization by dry heat.
Wherein, be closer to this utility model is high-temperature steam method and sterilization by dry heat, the high-temperature steam method that makes introductions all round below and the ultimate principle of sterilization by dry heat and shortcoming.
(1) ultimate principle of sterilization by dry heat is: medical waste poured out in Turnover Box, sends into treatment box in then putting it to platoon conveyer hopper.The treatment box first line of a couplet is connected to gas pumping cells in the reducing mechanism for pulverizing medical waste and suction process case, and pumping cells connects clean unit.Being provided with axle and agitating device in treatment box, treatment box outer bottom has cover layer.The deep fat material for continuous heating treatment box it is provided with between treatment box appearance and cover layer.15 minutes to 30 minutes treatment box high temperature sterilize time interval work.The lower section for the treatment of box is provided with conveyer belt with sides hopper, and the bottom for the treatment of box is tapered, and the bottom for the treatment of box is additionally provided with Dump gate.After sterilizing terminates, Dump gate is opened, and the medical waste through sterilizing naturally falls by weight and enters in conveyer belt with sides hopper, and the medical waste eventually passing sterilizing is transported to transport landfill in refuse bin.
During high temperature dry heat sterilization, not adding steam or moisture, heat is transmitted between rubbish by contact mode natural or by force.Rubbish is heated with naturally transmitting by the hot wall mainly utilizing the interior room for the treatment of box through conduction.Pending rubbish unit volume (0.9m3) bigger, although being provided with agitating device in treatment box, but heat transmission nevertheless suffers from limiting, the accepted heat of rubbish is uneven, and sterilizing efficiency is affected and then affects the sterilization stability of this technique.
In sterilization by dry heat, sterilization time 20 minutes, spout bag ETL estimated time of loading 10 minutes, after sterilizing completes, the transmission of medical waste, broken time are about 10 minutes.Treatment box is interval work, and treating capacity is low, during so using dry heat sterilization, can be done greatly by the volume for the treatment of box as far as possible, but being affected by the restriction of rubbish non-uniform temperature, and the treating capacity of medical waste is generally less than 5 ton day.There is presently no and find that the treating capacity of dry heat sterilization seldom has more than 10 ton day, be more not greater than the record of 20 ton day.
The technical problem that sterilization by dry heat exists is mainly: medical waste is open transmission during broken transmission, and waste odor is dispersed in surrounding, causes working environment excessively poor；Medical waste after sterilizing is also open transmission, and the medical waste uncontrollable discharge after sterilizing easily causes secondary pollution ecological environment；Final medical waste also needs to sanitary landfills.
(2) ultimate principle of high-temp steam sterilizing method is similar with sterilization by dry heat, and owing to the heat transmission medium of high-temp steam sterilizing method is the steam of heat, heat transference efficiency increases, but high-temp steam sterilizing method can produce waste liquid during sterilizing.In high-temp steam sterilizing method, the course of conveying of medical waste is to carry out in open environment, and the air pollution to surrounding is the most serious.High-temp steam sterilizing method falls within batch (-type) sterilizing, and treating capacity is little.
In sum, high-temp steam sterilizing method and sterilization by dry heat have individual common drawback, that is, the course of conveying of medical waste is carried out in open environment, in the emission of bad smell of medical waste to surrounding air and pollute environment.Poor working environment, the infected risk of staff are greatly the basic situation for the treatment of of!medical waste.
Utility model content
First purpose of the present utility model is to provide a kind of rubbish continuous sterilizer, and this device has that environmental pollution is little, sterilizing efficiency is high and the sterilizing advantage such as thoroughly.
Second purpose of the present utility model is to provide a kind of refuse disposal system, and this system has the advantages such as sterilization rate is high, environmental pollution is little.
This utility model is achieved in that
A kind of rubbish continuous sterilizer, including rubbish temporary storing bin, solid pump, conveying pipeline, medium ball and heat exchanger, the outlet of rubbish temporary storing bin connects with the entrance of solid pump, the entrance of conveying pipeline and the outlet of solid pump, medium ball is for mixing with rubbish and carrying along conveying pipeline, and heat exchanger is for heating conveying pipeline the rubbish transferring heat in conveying pipeline by conveying pipeline and medium ball.
A kind of refuse disposal system, including rubbish receiving bin, refuse grinder and rubbish continuous sterilizer, rubbish receiving bin is connected by the first refuse conveying pipe road with refuse grinder, refuse grinder is connected by the second refuse conveying pipe road with rubbish temporary storing bin, first refuse conveying pipe road and the second refuse conveying pipe road are the most vertically arranged, and rubbish receiving bin and rubbish temporary storing bin lay respectively at above and below refuse grinder.
The beneficial effect that this utility model realizes:
(1) this utility model original creation uses solid pump conveying garbage, be mixed in rubbish medium ball solve existing solid pump cannot the difficult problem of conveying garbage.
(2) power that this utility model carries using solid pump as rubbish, makes rubbish move along conveying pipeline, is heated to conveying pipeline by heat exchanger, rubbish completes sterilizing during moving in conveying pipeline, belong to sterilizing in closed environment, abnormal flavour or waste gas will not be produced, do not pollute the environment.
(3) existing rubbish sterilizing is all clearance-type, and treating capacity is little.This rubbish continuous apparatus of the present utility model due to, use pipeline conveying, rubbish can continuously pass through conveying pipeline, it is possible to continuous sterilization, garbage treatment quantity is big.
(4) relative to existing treatment box, the diameter of conveying pipeline of the present utility model is much smaller, and when heat passes to rubbish by conveying pipeline, heat transference efficiency is high, and rubbish sterilizing is thorough.
(5) this utility model uses medium ball to be mixed into rubbish to carry originally, and on the one hand medium ball plays a supporting role in rubbish, beneficially rubbish conveying, on the other hand, medium ball or the medium of heat transfer, can improve heat transference efficiency, and sterilizing is more thorough.
Accompanying drawing explanation
Fig. 1 shows the rough schematic view of the continuous sterilizer of this utility model embodiment 1；
Fig. 2 shows a-quadrant partial schematic diagram in Fig. 1；
Fig. 3 shows the schematic internal view during conveying pipeline son's conveying garbage in Fig. 2；
Fig. 4 shows the profile of the medium ball in Fig. 3；
Fig. 5 shows the schematic diagram of the connecting tube in Fig. 2；
Fig. 6 shows the rough schematic view when connecting tube in Fig. 2 is connected with straight tube and bend pipe；
Fig. 7 shows the schematic diagram of the refuse disposal system of this utility model embodiment 2；
Fig. 8 shows B region partial schematic diagram in Fig. 7；
Fig. 9 shows the rough schematic view of the refuse disposal system of this utility model embodiment 3；
Figure 10 shows C region partial schematic diagram in Fig. 9；
Figure 11 shows the thermal conductive oil pipeline connection diagram of the refuse disposal system of this utility model embodiment 3；
Figure 12 shows the compressed air line connection diagram of the refuse disposal system of this utility model embodiment 3；
Figure 13 shows the process gas pipeline connection diagram of the refuse disposal system of this utility model embodiment 3；
Figure 14 shows the lubricating fluid pipeline connection diagram of the refuse disposal system of this utility model embodiment 3；
Figure 15 shows the disinfectant solution pipeline connection diagram of the refuse disposal system of this utility model embodiment 3；
Figure 16 shows the schematic diagram of the refuse disposal system of this utility model embodiment 3；
Figure 17 shows the schematic diagram of the refuse disposal system of this utility model embodiment 4.
Wherein, the reference of Fig. 1～Figure 17 is:
Rubbish temporary storing bin 101；Solid pump 103；Conveying pipeline 105；Medium ball 107；First conveying worm 111；Output object temporary storing bin 113；Second conveying worm 115；Connecting tube 117；Annular projection 119；Oil guide groove 121；Lubricating fluid added holes 123；First heat exchange jacket 125；Tee T 127；Medium ball separator 129；Discharge duct 131；Medium ball conveying pipe 133；Output object conveying pipe 135；Separation platform 137；Medium ball detector 139；Medium ball flush trimmer 141；Rubbish receiving bin 201；Refuse grinder 203；First refuse conveying pipe road 205；Second refuse conveying pipe road 207；Turnover Box 209；Air sparger 211；Laser bag-breaking device 213；Dispel device 215；Opposite opened electric gate valve 216；Metal delivery tubes 217；Glass delivery tube 219；Metal detector 221；Metal removal device 223；Glass flush trimmer 225；Metal steriliser 227；Glass steriliser 229；Second heat exchange jacket 231；3rd heat exchange jacket 233；Aspiration channel 237；Compound plasma depurator 239；First disinfectant solution ejector 241；Moisture detector 243；Second disinfectant solution ejector 244；Fine crusher 245；Organic compound combustion device 247,303；Heat-conducting oil furnace 249；Compressed gas Arch-Breaking Device 251；Integral type screw air compressor 253；Solenoid electric valve group 255；Injection lubrication depressurized system 257；Petroleum pipeline 259；4th conveying worm 301；Rotary kiln 305；5th conveying worm 307；Cooler 309；Output object feed bin 311.
Detailed description of the invention
For making the purpose of this utility model embodiment, technical scheme and advantage clearer, below in conjunction with the accompanying drawing in this utility model embodiment, technical scheme in this utility model embodiment is clearly and completely described, obviously, described embodiment is a part of embodiment of this utility model rather than whole embodiments.Generally can with various different configurations arrange and design with the assembly of this utility model embodiment that illustrate described in accompanying drawing herein.
Therefore, the detailed description to the embodiment of the present utility model provided in the accompanying drawings is not intended to limit claimed scope of the present utility model below, but is merely representative of selected embodiment of the present utility model.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art are obtained under not making creative work premise, broadly fall into the scope of this utility model protection.
It should also be noted that similar label and letter represent similar terms in following accompanying drawing, therefore, the most a certain Xiang Yi accompanying drawing is defined, then need not it be defined further and explains in accompanying drawing subsequently.
Additionally, term " first ", " second ", " the 3rd " and " the 4th " is only used for describing purpose, and it is not intended that indicate or imply relative importance or the implicit quantity indicating indicated technical characteristic.
A kind of rubbish continuous sterilizer that this utility model provides includes: rubbish temporary storing bin, solid pump, conveying pipeline, medium ball and heat exchanger.The outlet of rubbish temporary storing bin connects with the entrance of solid pump, the entrance of conveying pipeline and the outlet of solid pump, medium ball is for mixing with rubbish and carrying along conveying pipeline, and heat exchanger is for heating conveying pipeline the rubbish transferring heat in conveying pipeline by conveying pipeline and medium ball.
Solid pump is also called hydraulic planger pump or hydraulic piston pump, and by hydraulic power Packet driven hydraulic jack, hydraulic jack advances conveying cylinder, exports the material in conveying cylinder to pipeline.It is generally divided into single plunger and double plunger, the typical 4 kinds of solid pump having German Putzmeister Inc. that represent, respectively: EKO single plunger pump, and tri-kinds of duplex plunger pumps of KOS, KOV, HSP.Solid pump is usually used in cement or building trade.
Rubbish of the present utility model is primarily referred to as medical waste, also includes house refuse, and other danger waste products also are able to use this rubbish continuous sterilizer of the present utility model to carry out sterilizing certainly.
In prior art, owing to conventional sterilization by dry heat and high-temp steam sterilizing method are all step, heat transfer efficiency in view for the treatment of box is limited, the volume for the treatment of box all can not be configured to the biggest, thus its treating capacity is less and is difficult to scale up, when treating capacity is bigger, major part have selected burning method and the high temperature pyrolytic cracking (HTP) of high pollution, and environment causes bigger destruction.
In medical waste and house refuse, key component is Organic substance, and Organic substance generally has certain elasticity, and is susceptible to compressive deformation, and then gets lodged in conveying pipeline, substantially belongs to the work that cannot complete with solid pump conveying garbage.Such as, medical waste composition and complexity thereof, mainly there are plastics (46%), fiber (24%), paper (8%), metal (6%), glass (5%) etc., these main components are elastic greatly cannot be directly with the KOS delivery pump of PM company, it is that rear medium pushes away front medium motion that KOS pump belongs to resilient plunger pump class medium motion character, and medical waste composition cannot realize.
After being mixed with rubbish by medium ball, become possibility with solid pump conveying garbage.
Medium ball is made up of hard material, mainly play a supportive role, space is formed between medium ball, rubbish is positioned at this space, so medium ball can disperse a part from the active force of solid pump, rubbish in conveying pipeline is not easy to pile up, and under the effect of carrying secretly of medium ball, the rubbish in conveying pipeline can move along conveying pipeline smoothly.
As preferably, medium ball is made up of the Heat Conduction Material of hard.Such as medium ball can be that metal is made.Medium ball, in addition to beneficially rubbish moves along conveying pipeline, also has another critically important effect, and that just transmits heat, and the conductive force of medium ball is much better than rubbish, and medium ball is blended among rubbish and can play the effect well transmitting heat.The main still high temperature sterilize of sterilized principle for germ of the present utility model, so the transmission of heat is critically important, after adding medium ball and rubbish mixing, sterilizing efficiency is effectively improved, and sterilizing is more thorough.
As preferably, the diameter of medium ball is less than the internal diameter of conveying pipeline, and the diameter of medium ball is more than the half of the internal diameter of conveying pipeline.
Medium ball needs to carry in conveying pipeline, and the diameter of medium ball must be less than the internal diameter of conveying pipeline.And the diameter of medium ball is more than the half of the internal diameter of conveying pipeline, it is to be in side by side relationship for the medium ball preventing two or more, if medium ball is located side by side in conveying pipeline, is then easier blocking in conveying pipeline comparatively speaking.When the diameter of medium ball is more than the half of the internal diameter of conveying pipeline, the medium ball in conveying pipeline substantially arranges along conveying pipeline with the form of wave, and rubbish and medium ball in conveying pipeline are all easier to carry along conveying pipeline.
As preferably, the 55%-65% of the internal diameter of a diameter of conveying pipeline of medium ball.
During the 55%-65% of the internal diameter of a diameter of conveying pipeline of medium ball, the quantity of refuse of the conveying pipeline conveying of unit length is most, and the most smooth and easy during rubbish conveying, is also not easy blocking when being delivered to bend pipe.
As preferably, the inside of medium ball has the hollow structure for alleviating medium ball quality.
On the premise of ensureing that deformation is less likely to occur medium ball, hollow structure will be made in medium ball or selection has the medium ball of hollow structure and advantageously reduces the quality of medium ball, be conducive to improving the Effective power of solid pump.
As preferably, conveying pipeline is tightly connected by multiple straight tubes and forms, or conveying pipeline is formed by connecting by multiple straight tubes and multiple bend pipe；The sidewall of conveying pipeline or junction are provided with lubricating fluid added holes.
The diameter of conveying pipeline is much smaller size compared with existing treatment box, but the length dimension of conveying pipeline is bigger.Conveying pipeline entirety can be arranged along a straight line, it is also possible to tortuous layout.Owing to being arranged along a straight line, needs take bigger space, it is tortuous layout in the best manner, during tortuous layout, bend pipe is needed to connect, and rubbish is by bigger than by straight tube difficulty during bend pipe, so preferably spraying lubricating fluid in conveying pipeline in pipe bent position, reduce the frictional force between rubbish and conveying pipeline, naturally it is also possible to spray lubricating fluid at other positions of conveying pipeline.
Lubricating fluid can use the machine oil of lubrication, vaseline, the liquid wax that major part Organic substance, such as mechanical field are common, it is also possible to uses discarded machine oil as lubricating fluid.
As preferably, connected by connecting tube between straight tube and bend pipe, the inwall of connecting tube has annular projection, the end of straight tube and bend pipe is respectively arranged at the opposite sides of annular projection, annular projection have for by lubricating fluid along connecting tube circumference guide oil guide groove, lubricating fluid added holes connects with oil guide groove.
As preferably, heat exchanger includes that the first heat exchange jacket, the first heat exchange jacket are arranged at the outer wall of conveying pipeline, and the inside of the first heat exchange jacket has the circulation cavity of heat transferring medium, and the first heat exchange jacket has heat transferring medium entrance and heat transferring medium outlet.
Conveying pipeline is complications when arranging, adjacent heat exchange jacket can be together in series use.
The treating capacity of this rubbish continuous sterilizer can be regulated by the output of regulation solid pump, it is also possible to is regulated by the length of the conveying pipeline being enclosed with heat exchange jacket of rubbish process.
As preferably, the outlet of conveying pipeline is connected with output object temporary storing bin by the first discharge duct, and the middle part of conveying pipeline connects has tee T, tee T to have discharge port, and discharge port is connected with output object temporary storing bin by the second discharge duct.
As preferably, the exit of conveying pipeline is provided with medium ball separator, medium ball separator includes discharge duct, medium ball conveying pipe and output object conveying pipe, output object conveying pipe connects with output object temporary storing bin, medium ball conveying pipe connects with rubbish temporary storing bin, and medium ball is transported to rubbish temporary storing bin by medium ball conveying pipe.
As preferably, medium ball separator also includes separation platform, discharge duct is vertically arranged, medium ball conveying pipe may be contained within the lower section of discharge duct with output object conveying pipe and connects with discharge duct, separation platform is positioned at discharge duct, and separation platform is inclined relative to horizontal setting and for guiding medium ball to move in medium ball conveying pipe.
As preferably, medium ball separator also includes medium ball detector and medium ball flush trimmer, medium ball detector is arranged at the outside of discharge duct and for detecting medium ball, and medium ball flush trimmer includes compressed gas shower nozzle, and the outlet of compressed gas shower nozzle is arranged towards separation platform.
As preferably, the pipeline of medium ball conveying pipe being provided with the first conveying worm for providing conveying power to medium ball, the entrance and exit of the first conveying worm all connects with medium ball conveying pipe.
As preferably, the bottom of rubbish temporary storing bin is provided with the second conveying worm, and the entrance of the second conveying worm connects with rubbish temporary storing bin, and the outlet of the second conveying worm connects with the entrance of solid pump.
A kind of refuse disposal system that this utility model provides, including rubbish receiving bin, refuse grinder and rubbish continuous sterilizer, rubbish receiving bin is connected by the first refuse conveying pipe road with refuse grinder, refuse grinder is connected by the second refuse conveying pipe road with rubbish temporary storing bin, first refuse conveying pipe road and the second refuse conveying pipe road are the most vertically arranged, and rubbish receiving bin and rubbish temporary storing bin lay respectively at above and below refuse grinder.
Domestic medical waste is to be not classified as the main mode that loads in mixture, and after high temperature dry heat sterilization technology sterilizing, output object is also that various types of materials mixture prior art cannot separate the necessary sanitary landfills of utilization, causes waste to pollute environment.
As preferably, refuse disposal system also includes device for separation of waste, device for separation of waste is arranged between refuse grinder and rubbish temporary storing bin, device for separation of waste includes metal delivery tubes, glass delivery tube, for detecting the metal detector of metal, for rejecting the metal removal device of metal and for rejecting the glass flush trimmer of glass, metal delivery tubes is all obliquely installed with glass delivery tube and connects with the second refuse conveying pipe road, metal removal device is arranged at metal delivery tubes and the junction in the second refuse conveying pipe road, glass flush trimmer is arranged at the junction of glass delivery tube and the second refuse conveying pipe road.
As preferably, metal delivery tubes connects has metal steriliser, metal steriliser to include metal sterilization tank and the second heat exchange jacket；Glass delivery tube road connects has glass steriliser, glass steriliser to include glass sterilization tank and the 3rd heat exchange jacket.
As preferably, rubbish receiving bin has feeding mouth, is provided with air sparger at feeding mouth, and air sparger is for producing the air curtain being isolated from the outside the inside of rubbish receiving bin.
As preferably, being provided with laser bag-breaking device and dispel device in the first refuse conveying pipe road, laser bag-breaking device has the laser head launching laser beam, and dispelling utensil has the shower nozzle of jet compression gas.
As preferably, the first disinfectant solution ejector and moisture detector it is provided with in rubbish temporary storing bin, disinfectant solution ejector electrically connects with moisture detector, and moisture detector is for detecting the humidity in rubbish temporary storing bin and sending the control signal of injection disinfectant solution to disinfectant solution ejector.
As preferably, in rubbish receiving bin and/or the first refuse conveying pipe road, it is provided with the second disinfectant solution ejector.
As preferably, refuse disposal system also includes combustion system, combustion system includes fine crusher, organic compound combustion device and heat-conducting oil furnace, the outlet of conveying pipeline is connected with output object temporary storing bin by the first discharge duct, the middle part of conveying pipeline connects tee T, tee T has discharge port, and discharge port is connected with output object temporary storing bin by the second discharge duct；The outlet of output object temporary storing bin connects with fine crusher, and fine crusher has the first outlet connected with organic compound combustion device, and organic compound combustion device is for heating the heat transferring medium in heat-conducting oil furnace, and heat-conducting oil furnace connects with heat exchanger.
A kind of waste disposal method that this utility model provides, comprises the following steps:
Blend step, is mixed to get garbage mixture by rubbish and medium ball in rubbish temporary storing bin；
Sterilization steps, utilizes solid pump to provide power to make garbage mixture carry along conveying pipeline, heats the outer wall of conveying pipeline during garbage mixture carries along conveying pipeline, and garbage mixture completes sterilizing during carrying along conveying pipeline.
As preferably, during garbage mixture carries along conveying pipeline, compartment of terrain sprays lubricating fluid in conveying pipeline.
Time and the interlude of injection lubricating fluid can be set according to the needs of technological design.
As preferably, detecting the humidity of garbage mixture before sterilization steps, the humidity of garbage mixture, less than when setting 40%, sprays disinfectant solution to garbage mixture.
The humidity of garbage mixture is too low is unfavorable for that rubbish carries.On the one hand sterilization can increase the water content of garbage mixture, on the other hand can play the effect of sterilizing.
As preferably, the bottom of rubbish temporary storing bin and/or the bottom of output object temporary storing bin are provided with compressed gas Arch-Breaking Device.
As preferably, after rubbish completes sterilizing, medium ball is discharged from conveying pipeline, is separated by medium ball and deliver in rubbish temporary storing bin and be used for again mix with rubbish from rubbish mixes.
As preferably, before blend step, also include destruction step and separating step；Destruction step is: the sack of parcel rubbish is carried out broken bag, is then dispelled by rubbish, then by refuse breaking；Separating step is: the metal in rubbish and glass after crushing are separated, sterilization treatment independent to metal and glass；Broken bag and separation are all carried out in the pipeline sealed.
As preferably, the metal after sterilizing, glass and rubbish are packed respectively and marks.
Embodiment 1, sees Fig. 1～Fig. 6.
Present embodiments provide a kind of rubbish continuous sterilizer, as it is shown in figure 1, this rubbish continuous sterilizer includes rubbish temporary storing bin 101, solid pump 103, conveying pipeline 105, medium ball 107, heat exchanger, the first conveying worm, output object temporary storing bin 113 and the second conveying worm 115.
The top of rubbish temporary storing bin 101 is provided with entrance and bottom is provided with outlet, second conveying worm 115 be arranged on rubbish temporary storing bin 101 bottom and with rubbish temporary storing bin 101 outlet, the outlet of the second conveying worm 115 connects with the entrance of solid pump 103.Rubbish in rubbish temporary storing bin 101 is mainly carried by the effect of the second conveying worm 115 to solid pump 103, ensure have rubbish successively to enter solid pump 103, improve work efficiency and reliability, naturally it is also possible to use other structures to substitute the second conveying worm 115.
The entrance of conveying pipeline 105 and the outlet of solid pump 103.During with solid pump 103 conveying garbage, first rubbish subject to sterilization and medium ball 107 being mixed in rubbish temporary storing bin 101, then rubbish and medium ball 107 carry along conveying pipeline 105.
Medium ball 107 is made up of the Heat Conduction Material of hard.Medium ball 107 is preferably made of metal, such as, be made of stainless steel.The diameter of medium ball 107 is less than the internal diameter of conveying pipeline 105, and the diameter of medium ball 107 is more than the half of the internal diameter of conveying pipeline 105.Reasonable solid yardage case is, the 55%-65% of the internal diameter of a diameter of conveying pipeline 105 of medium ball 107, the quantity of refuse that such dimension scale makes the conveying pipeline 105 of unit length carry is most, and the most smooth and easy during rubbish conveying, is also not easy blocking when being delivered to bend pipe.
As shown in Figure 3, the diameter of medium ball 107 is about the 60% of the internal diameter of conveying pipeline 105, medium ball 107 in conveying pipeline 105 substantially arranges along conveying pipeline 105 with the form of wave, and rubbish and medium ball 107 in conveying pipeline 105 are all easier to carry along conveying pipeline 105.
As shown in Figure 4, the inside of medium ball 107 has the hollow structure for alleviating medium ball 107 mass.On the premise of ensureing that deformation is less likely to occur medium ball 107, hollow structure will be made in medium ball 107 or selection has the medium ball 107 of hollow structure and advantageously reduces the quality of medium ball 107, be conducive to improving the Effective power of solid pump 103.
As in figure 2 it is shown, conveying pipeline 105 is formed by connecting by multiple straight tubes and multiple bend pipe, conveying pipeline 105 is tortuous layout on the whole, is connected by connecting tube 117 between straight tube and bend pipe.As shown in Figure 5, the inwall of connecting tube 117 has annular projection 119, the end of straight tube and bend pipe is respectively arranged at the opposite sides of annular projection 119, annular projection 119 have for by lubricating fluid along connecting tube 117 circumference guide oil guide groove 121, lubricating fluid added holes 123 connects with oil guide groove 121.
The diameter of conveying pipeline 105 is much smaller size compared with existing treatment box, but the length dimension of conveying pipeline 105 is bigger.Conveying pipeline 105 is tortuous to be arranged, can reduce the space taken.
But after arranging bend pipe, bringing new problem, rubbish is by bigger than by straight tube difficulty during bend pipe.So arranging lubricating fluid added holes 123 and for spraying lubricating fluid in bend pipe in pipe bent position.Injection lubricating fluid can reduce the frictional force between rubbish and conveying pipeline 105, naturally it is also possible to spray lubricating fluid at other positions of conveying pipeline 105.Lubricating fluid can use the machine oil playing lubrication that major part Organic substance, such as mechanical field are common, it is also possible to uses discarded machine oil as lubricating fluid.
Heat exchanger is for heating conveying pipeline 105 and transferring heat to the rubbish in conveying pipeline 105 and medium ball 107 by conveying pipeline 105, and medium ball 107 can also transfer heat to rubbish simultaneously.Medium ball 107, in addition to beneficially rubbish moves along conveying pipeline 105, also has another critically important effect, and that just transmits heat, and the conductive force of medium ball 107 is much better than rubbish, and medium ball 107 is blended among rubbish and can play the effect well transmitting heat.The main still high temperature sterilize of sterilized principle for germ of the present utility model, so the transmission of heat is critically important, after adding medium ball 107 and rubbish mixing, sterilizing efficiency is effectively improved, and sterilizing is more thorough.
As in figure 2 it is shown, heat exchanger includes that the first heat exchange jacket 125, the first heat exchange jacket 125 are arranged at the outer wall of conveying pipeline 105, for the ease of installing, the first heat exchange jacket 125 is arranged at the outer wall of straight tube of conveying pipeline 105 specifically.The inside of the first heat exchange jacket 125 has the circulation cavity of heat transferring medium, and the first heat exchange jacket 125 has heat transferring medium entrance and heat transferring medium outlet.The straight pipe parallel of conveying pipeline 105 is arranged, and adjacent straight tube is close together, so the first adjacent heat exchange jacket 125 is serially connected.
The treating capacity of this rubbish continuous sterilizer can be regulated by the output of regulation solid pump 103, it is also possible to is regulated by the length of the conveying pipeline 105 being enclosed with heat exchange jacket of rubbish process.The outlet of conveying pipeline 105 is connected with output object temporary storing bin 113 by the first discharge duct 131, and the middle part of conveying pipeline 105 connects has tee T 127, tee T 127 to have discharge port, and discharge port is connected with output object temporary storing bin 113 by the second discharge duct 131.In the present embodiment, tee T 127 is substantially disposed in the middle part of the length of conveying pipeline 105, can be switched the trend of rubbish by tee T 127, it may also be said to be can to change rubbish sterilization time in conveying pipeline 105 by tee T 127, the motion path of rubbish is long, then sterilization time is long.Rubbish is when discharge port is discharged, and sterilization time is shorter, and rubbish is when the outlet of conveying pipeline 105 is discharged, and sterilization time is longer.
As illustrated in fig. 1 and 2, the exit of conveying pipeline 105 is provided with medium ball separator 129, and medium ball separator 129 includes discharge duct 131, medium ball conveying pipe 133, output object conveying pipe 135, separation platform 137, medium ball detector 139 and medium ball flush trimmer 141.Output object conveying pipe 135 connects with output object temporary storing bin 113, and medium ball conveying pipe 133 connects with rubbish temporary storing bin 101, and medium ball 107 is transported to rubbish temporary storing bin 101 by medium ball conveying pipe 133.Discharge duct 131 is vertically arranged, medium ball conveying pipe 133 may be contained within the lower section of discharge duct 131 with output object conveying pipe 135 and connects with discharge duct 131, separation platform 137 is positioned at discharge duct 131, and separation platform 137 is inclined relative to horizontal setting and for guiding medium ball 107 to move in medium ball conveying pipe 133.When medium ball is metal, medium ball detector 139 is the most also metal detector 221, medium ball detector 139 is arranged at the outside of discharge duct 131 and for detecting medium ball 107, and medium ball flush trimmer 141 includes that compressed gas shower nozzle, the outlet of compressed gas shower nozzle are arranged towards separation platform 137.
At output object conveying pipe 135, medium ball detector 139 and medium ball flush trimmer 141 are installed, in the present embodiment, medium ball 107 is the metal ball of internal concrete hollow structure, medium ball detector 139 is metal detector, if output object conveying pipe 135 is made of metal completely, metal detector can be affected normally work, so output object conveying pipe 135 part is made up (can certainly be all to be made up of nonmetallic materials) of nonmetallic materials, medium ball detector 139 is installed on the non-metallic part of output object conveying pipe 135.Rubbish and medium ball 107 are when output object conveying pipe 135, medium ball detector 139 detects medium ball 107, then control signal is sent to medium ball flush trimmer 141, medium ball flush trimmer 141 specifically uses compressed gas shower nozzle, compressed gas shower nozzle receives and sprays gases at high pressure after the control signal of medium ball detector 139, medium ball 107 can be blown in medium ball conveying pipe 133 by gases at high pressure, medium ball 107 is returned in rubbish temporary storing bin 101 through medium ball conveying pipe 133, and medium ball 107 can recycle.
Being provided with the first conveying worm 111 for providing conveying power to medium ball 107 on the pipeline of medium ball conveying pipe 133, the entrance and exit of the first conveying worm 111 all connects with medium ball conveying pipe 133.If medium ball conveying pipe 133 relatively with tilt during horizontal plane, and the entrance of medium ball conveying pipe 133 is higher than exporting, then can the first conveying worm 111.
Rubbish in course of conveying, sprays lubricating fluid at pipe bent position and straight tube, makes to move pressure at this and quickly reduce in conveying pipeline 105, and system pressure declines.Such as KOS pump is under specified output pressure (12Mpa), the length of conveying pipeline 105 can be designed into more than 60 meters, in conveying pipeline 105, spray lubricating fluid be possible not only to make rubbish mobile more smooth and easy in conveying pipeline 105, can also extend the design length of conveying pipeline 105, the rubbish processed in conveying pipeline 105 is more.In sealing conveying pipeline 105, the output of continuous moving sterilization time, rubbish length of motion route and solid pump 103 has relation, under conditions of the rated output of solid pump 103, the length of the conveying pipeline 105 being provided with heat exchanger determines sterilization treatment amount, and treating capacity can be the biggest in theory.The treating capacity of such as KOS pump can reach more than 20 ton day.
In high-temp steam sterilizing technology, rubbish is resting state in sterile chamber, and its rubbish central part high-temperature steam is difficult to penetrate and causes dead angle sterilization rate unstable；Though high temperature xeothermic technology sterilization technology has agitating device in sterilization treatment case, in finite time, it is extremely difficult to sterilization treatment chamber interior wall temperature in the big situation of plot ratio, makes sterilizing efficiency unstable.
This utility model is to carry out heat exchange, the little (0.017m of conveying pipeline 105 sectional area with heat exchanger2) exchange of the least rubbish of plot ratio and the inwall heat in inner tube of heat exchanger road is highly uniform, and heat exchange is jointly carried out with medium ball, there is not Dead Core Problems between rubbish.When medium ball 107 is metal simultaneously, heat transference efficiency is high, and after medium ball 107 and conveying pipeline 105 carry out heat exchange, medium ball 107 again carries out heat exchange again to rubbish, so sterilization rate is highly stable, sterilization effect is reliable.
Embodiment 2, sees Fig. 7 and Fig. 8.
Present embodiments providing a kind of refuse disposal system, the refuse disposal system of the present embodiment includes the rubbish continuous sterilizer of embodiment 1, and the structure do not mentioned in the present embodiment refers to the description of embodiment 1.
As shown in Figure 7 and Figure 8, a kind of refuse disposal system includes rubbish receiving bin 201, refuse grinder 203 and rubbish continuous sterilizer, rubbish receiving bin 201 is connected by the first refuse conveying pipe road 205 with refuse grinder 203, refuse grinder 203 is connected by the second refuse conveying pipe road 207 with rubbish temporary storing bin 101, first refuse conveying pipe road 205 and the second refuse conveying pipe road 207 are the most vertically arranged, and rubbish receiving bin 201 and rubbish temporary storing bin 101 lay respectively at above and below refuse grinder 203.Being additionally provided with Turnover Box 209 and the control system of Turnover Box 209 at the feeding mouth of rubbish receiving bin 201, Turnover Box 209 can enter in rubbish receiving bin 201 from the feeding mouth of rubbish receiving bin 201 and dump rubbish.The Turnover Box 209 filling medical waste is shifted onto the reservation position of rubbish inclinator, and rubbish can be poured in rubbish receiving bin 201 by start button system automatically.
Air sparger 211 it is provided with at the feeding mouth of rubbish receiving bin 201, air sparger 211 is used for producing air curtain, the inside of rubbish receiving bin 201 can be isolated from the outside by air curtain, and air curtain does not interferes with rubbish yet and enters rubbish receiving bin 201 from this feeding mouth simultaneously.
Being provided with laser bag-breaking device 213 in first refuse conveying pipe road 205 and dispel device 215, laser bag-breaking device 213 has the laser head launching laser beam, dispels device 215 and has the shower nozzle of jet compression gas.When the laser material position controller of laser bag-breaking device 213 detects that material position is the fullest, and send control signal and make the opposite opened electric gate valve 216 below rubbish receiving bin 201 close, simultaneously, dynamic rotation supports and rotarily drives the rotation of internal layer stainless steel coil, laser bag-breaking device 213 starts to launch certain energy laser (200W), internal layer stainless steel coil designs three fixed range flutings, laser beam is injected in the outer bag of rubbish by internal layer fluting, rubbish outer bag (usually plastic material) rapid melting under laser high-energy effect, when internal layer stainless steel coil rotates, laser can rotate around refuse bag, rubbish outer bag is melted thorough broken bag by 360 degree.After broken bag, opposite opened electric gate valve 216 is opened, in the first refuse conveying pipe road 205, dispel device 215 rubbish is dispelled with homogenizing after, rubbish enters refuse grinder 203 and crushes, and then broken rubbish enters rubbish temporary storing bin 101 through the second refuse conveying pipe road 207.
Embodiment 3, sees Fig. 9～Figure 16.
Present embodiments providing a kind of refuse disposal system, the present embodiment and differing only in of embodiment 2 are additionally provided with device for separation of waste, and the structure do not mentioned in the present embodiment refers to the description of embodiment 1 and 2.
Domestic medical waste is to be not classified as the main mode that loads in mixture, and after high temperature dry heat sterilization technology sterilizing, output object is also that various types of materials mixture prior art cannot separate the necessary sanitary landfills of utilization, causes waste to pollute environment.
In order to overcome the problems referred to above, the refuse disposal system of the present embodiment also includes device for separation of waste.As shown in Figure 9 and Figure 10, device for separation of waste is arranged between refuse grinder 203 and rubbish temporary storing bin 101.Device for separation of waste include metal delivery tubes 217, glass delivery tube 219, for detecting the metal detector 221 of metal, for rejecting the metal removal device 223 of metal and for rejecting the glass flush trimmer 225 of glass.Metal delivery tubes 217 is all obliquely installed with glass delivery tube 219 and connects with the second refuse conveying pipe road 207, metal removal device 223 is arranged at metal delivery tubes 217 and the junction in the second refuse conveying pipe road 207, and glass flush trimmer 225 is arranged at glass delivery tube 219 and the junction in the second refuse conveying pipe road 207.
Second refuse conveying pipe road 207 is made up of nonmetallic materials, metal removal device 223 is installed in the crossing of the second refuse conveying pipe road 207, metal delivery tubes 217 and glass delivery tube 219, metal removal device 223 can be analogous to the compressed gas shower nozzle as medium ball separator, it can also be triple channel flap valve, it is preferred to use triple channel flap valve.Control signal is sent to triple channel flap valve when metal detector 221 detects metal, triple channel flap valve makes the entrance of metal delivery tubes 217 open, the rubbish being mingled with metal on a small quantity enters in metal delivery tubes 217 from the second conveyance conduit 207, metal delivery tubes 217 connects has metal steriliser 227, metal steriliser 227 to include metal sterilization tank and the second heat exchange jacket 231.Remaining in second refuse conveying pipe road 207 is organic principle and glass, it is provided with horizontal plate in second refuse conveying pipe road 207, organic principle enters rubbish temporary storing bin 101, glass rests in the second refuse conveying pipe road 207 constantly to be assembled on horizontal plate, when reaching some, Super-sonic Level Cell sends signal and makes high pressure gas glass flush trimmer 225 work, and glass flows into glass delivery tube 219 road.Glass delivery tube 219 road connects has glass steriliser 229, glass steriliser 229 to include glass sterilization tank and the 3rd heat exchange jacket 233.
As shown in figure 13, rubbish temporary storing bin 101, output object temporary storing bin 113 are all connected with compound plasma depurator 239 by aspiration channel 237 with rubbish receiving bin 201, wind Parker's blower fan is installed on aspiration channel 237 simultaneously, gas in rubbish temporary storing bin 101, output object temporary storing bin 113 and rubbish receiving bin 201 can be extracted in compound plasma depurator 239 by wind Parker's blower fan, and produces certain negative pressure in making rubbish temporary storing bin 101, output object temporary storing bin 113 and rubbish receiving bin 201.
Dust is stopped exsiccator technology by this utility model and plasma for purification technology groups synthesizes new tail gas clean-up technology (compound plasma depurator 239).
Dust stops exsiccator and can moisture and bulky grain thing stop in tail gas, and plasma purifier has degraded and deodorization widely to stench, abnormal flavour, volatile organic matter.Lower temperature plasma technology processes the principle of pollutant: under the effect of extra electric field, what medium discharge produced takes energy electron bombardment contaminant molecule in a large number, make it ionize, dissociate and excite, the most just the physics of series of complex, chemical reaction have been caused, complicated macromolecule contaminant is made to be changed into simple little molecule safe material, or make poisonous and harmful substance be transformed into the nontoxic or material of the low evil of low toxicity, the removal so that pollutant are degraded.
Degraded volatile organic contaminant (VOCs) traditional processing method such as absorption and sorption, condense and burning etc., VOCs for low concentration is difficulty with, and there is the problem that catalyst easily inactivates in photocatalytic degradation VOCs, utilize Low Temperature Plasma Treating VOCs can not be limited by above-mentioned condition, there is potential advantage, open up the new technique of medical waste sterilization treatment vent gas treatment.
Metal detector 221 and metal detection executor thereof are mature technologies, are used in the separation of medical waste first.From medical waste, separation of glasses is to utilize rubbish negative pressure transportation principle, after in medical waste, metal is separated, and the maximum (2.5g/cm of glass density in residual components3), other component density is 0.85～1.50g/cm3Between, adjust wind Parker's fan delivery, by in low-density composition negative pressure transportation to rubbish temporary storing bin 101, category of glass composition is gathered on structure platform, when reaching some, ultrasonic broken level-sensing device detects that signal is connected high-pressure glass flush trimmer 225 and released high-speed gas, and category of glass composition is blown into sterilizing in glass steriliser 229.
As shown in figure 15, rubbish temporary storing bin 101 is interior or the second conveying worm 115 is provided with the first disinfectant solution ejector 241 and moisture detector 243, disinfectant solution ejector electrically connects with moisture detector 243, and moisture detector 243 is for detecting the humidity in rubbish temporary storing bin 101 and sending the control signal of injection disinfectant solution to disinfectant solution ejector.
Residue organic waste fully enters in rubbish temporary storing bin 101, and organic waste and medium ball 107 are mixed by the second conveying worm 115, during the most manually valve enters solid pump 103.Moisture detector 243 (moisture detector 243 specifically have employed the online moisture monitor of MIR) it is mounted with in the second conveying worm 115, when monitor value is less than automatically compensating disinfectant solution regulation moisture value when setting numerical value, rubbish water content is made to meet the requirement of solid pump 103.
In order to avoid the pathogenic bacteria in rubbish produces impact to equipment, in rubbish receiving bin 201 and the first refuse conveying pipe road 205, it is provided with the second disinfectant solution ejector 244.
As shown in figure 11, this refuse disposal system also includes combustion system, combustion system includes fine crusher 245, organic compound combustion device 247 and heat-conducting oil furnace 249, the outlet of output object temporary storing bin 113 connects with fine crusher 245, fine crusher 245 has the first outlet connected with organic compound combustion device 247, organic compound combustion device 247 is for heating the heat transferring medium in heat-conducting oil furnace 249, and heat-conducting oil furnace 249 connects with heat exchanger.Heat-conducting oil furnace 249 connects with first heat exchange jacket the 125, second heat exchange jacket 231 and the 3rd heat exchange jacket 233.Additionally, this processing system also includes that bedding and clothing steriliser, the outer wall of bedding and clothing steriliser are provided with the 4th heat exchange jacket, the 4th heat exchange jacket also connects with heat-conducting oil furnace 249.
The output object of this processing system is raw material and organic-fuel；It is a kind of green, environmental protection, energy-conservation subversiveness new technique.
It is little (less than 3000m that non-burning method process gas produces total amount3/ h) below and complicated component, major pollutants have chloride, sulfide, VOCs, stench etc..
High temperature dry heat sterilization technology uses high-voltage electrostatic dust separator, high-temp steam sterilizing technology to use fine dedusting technology；High-voltage electrostatic purification device principle: dirty particulate matter is captured due to mechanical collision, detention on homogenizing plate.When tail gas stream enters high-voltage electrostatic field, under the effect of high voltage electric field, tail gas ionizes, and mist of oil is charged, and major part is degraded carbonization；Small part oil or fat particles moves to the positive/negative plate of electric field under the electric field force and airflow function of absorption electric field and is collected on pole plate and flows to collection tray under the effect of self gravitation, discharges through passage；But it is inconspicuous for volatile organic contaminant (VOCs) and stench high-voltage electrostatic dust separator clean-up effect, in actual use owing to tail gas containing large quantity of moisture, make high-voltage electrostatic dust separator insulation variation electric wiring often burn out and make exhaust gas purification system cisco unity malfunction.
As shown in figure 12, in rubbish receiving bin the 201, first refuse conveying pipe road 205 and the second conveying worm 115, it is mounted on compressed gas Arch-Breaking Device 251, medium ball flush trimmer 141 (compressed gas shower nozzle) is installed in medium ball separation pipeline.Compressed gas Arch-Breaking Device 251 and medium ball flush trimmer 141 are all connected with integral type screw air compressor 253, and are controlled pressure and the distribution of compressed gas by solenoid electric valve group 255.
As shown in figure 14, this refuse disposal system of the present embodiment also includes injection lubrication depressurized system 257, the petroleum pipeline 259 of injection lubrication depressurized system 257 is connected with the lubricating fluid added holes 123 on conveying pipeline 105, injection lubrication depressurized system 257 can spray lubricating fluid at regular time and quantity in conveying pipeline 105, reduce conveying pipeline 105 internal pressure, improve rubbish transfer efficiency.Figure 16 is the overall schematic diagram of the refuse disposal system of the present embodiment.
The present embodiment additionally provides a kind of waste disposal method, comprises the following steps:
Destruction step is: the sack of parcel rubbish is carried out broken bag, is then dispelled by rubbish, then by refuse breaking.
Separating step is: the metal in rubbish and glass after crushing are separated, sterilization treatment independent to metal and glass；Broken bag and separation are all carried out in the pipeline sealed.
Blend step: rubbish and medium ball are mixed to get garbage mixture in rubbish temporary storing bin 101；Detecting the humidity of garbage mixture before sterilization steps, the humidity of garbage mixture, less than when setting 40%, sprays disinfectant solution to garbage mixture.
Sterilization steps: utilize solid pump 103 to provide power to make garbage mixture carry along conveying pipeline 105, heating the outer wall of conveying pipeline 105 during garbage mixture carries along conveying pipeline 105, garbage mixture completes sterilizing during carrying along conveying pipeline 105.During garbage mixture carries along conveying pipeline 105, compartment of terrain sprays lubricating fluid in conveying pipeline 105.
Medium ball recycling step: after rubbish completes sterilizing, medium ball is discharged from conveying pipeline 105, is separated by medium ball and deliver in rubbish temporary storing bin 101 and be used for again mix with rubbish from rubbish mixes.
Marking step: the metal after sterilizing, glass and rubbish are packed respectively and marks.Input computer management for future reference system after regenerant being set up sample program and carrying out laser marking, it is simple to the disposition of inquiry rubbish and tracking rubbish, concrete labelling can be Quick Response Code, numbering and electronic tag etc..Regenerant meets existing policy and the China's actual conditions of country, and after making medical waste sterilizing, regenerant utilizes and has good grounds, and periodically spot-check sterilization quality with chemical detection agent (biological detection agent).
Embodiment 4, sees Figure 17.
Present embodiments providing a kind of rubbish disinfection system, the present embodiment adds hazardous waste process line with differing only in of embodiment 3, and the structure do not mentioned in the present embodiment refers to the description of embodiment 3.
As shown in figure 17, hazardous waste process line includes the 4th conveying worm 301, organic compound combustion device 303, rotary kiln the 305, the 5th conveying worm 307, cooler 309 and output object feed bin 311.The entrance of rotary kiln 305 and the outlet of the 5th conveying worm 307 connect, the entrance of the 5th conveying worm 307 is connected with conveying pipeline 105, organic compound combustion device 303 improves heat energy to rotary kiln 305, the entrance and exit of the 4th conveying worm 301 is connected with fine crusher 245 and organic compound combustion device 303 respectively, and the rubbish after in small, broken bits is transported in organic compound combustion device 303 by the 4th conveying worm 301.The entrance and exit of cooler 309 is connected with rotary kiln 305 and output object feed bin 311 respectively.
The output object of high-temp steam sterilizing technology is through manually moving in sterile chamber elevator in sterilizing indoor metal dolly, subsequently into crusher in crushing, pull-out landfill in output object flows to dumper skip after broken, output object transports, crushes is all, what open environment completed, environment to be produced secondary pollution, affects operative employee physically and mentally healthy.
In the xeothermic technology of high temperature, output object is released in sterilization tank and is flowed to conveyer belt with sides, then flowing into rubbish Turnover Box 209 interior (or flowing directly in tipper carriage) is the most all open transport discharge way, dry heat sterilization technology is when actual motion simultaneously, in output object, low melting point melts in sterilization process and is bonded on sterilization tank inwall and on paddle, after sterilizing, output object cannot lean on weight to flow out at all, by manpower, output object must be extracted, making operation carry out under very severe environment, operative employee is the most painful.
This utility model technology output object flows in output object storehouse under vacuum cavitations, wind Parker's fan frequency conversion is had to control negative pressure number, output object is made easily to flow in output object storehouse, gases at high pressure arch breaking apparatus and DWG it is provided with bottom output object storehouse, by output object by the interior heat-conducting oil furnace 249 confession organic-fuel in system of reversal valve closed conveying to organic compound combustion device 245, unnecessary output object is deposited as standby organic-fuel is standby.
The foregoing is only preferred embodiment of the present utility model, be not limited to this utility model, for a person skilled in the art, this utility model can have various modifications and variations.All within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, within should be included in protection domain of the present utility model.
Claims (19)
1. a rubbish continuous sterilizer, it is characterized in that, including rubbish temporary storing bin, solid pump, conveying pipeline, medium ball and heat exchanger, the outlet of described rubbish temporary storing bin connects with the entrance of described solid pump, the entrance of described conveying pipeline and the outlet of described solid pump, described medium ball is for mixing with rubbish and carrying along conveying pipeline, and described heat exchanger is for heating conveying pipeline the rubbish transferring heat in conveying pipeline by conveying pipeline and medium ball.
Rubbish continuous sterilizer the most according to claim 1, it is characterised in that the 55%-65% of the internal diameter of a diameter of described conveying pipeline of described medium ball.
Rubbish continuous sterilizer the most according to claim 2, it is characterised in that the inside of described medium ball has the hollow structure for alleviating medium ball quality, described medium ball is made up of the Heat Conduction Material of hard.
Rubbish continuous sterilizer the most according to claim 1, it is characterized in that, described conveying pipeline is formed by connecting by multiple straight tubes and multiple bend pipe, connected by connecting tube between described straight tube and described bend pipe, the inwall of described connecting tube has annular projection, the end of described straight tube and described bend pipe is respectively arranged at the opposite sides of described annular projection, described annular projection have for by lubricating fluid along connecting tube circumference guide oil guide groove, described lubricating fluid added holes connects with described oil guide groove.
Rubbish continuous sterilizer the most according to claim 1, it is characterized in that, described heat exchanger includes the first heat exchange jacket, described first heat exchange jacket is arranged at the outer wall of described conveying pipeline, the inside of described first heat exchange jacket has the circulation cavity of heat transferring medium, and described first heat exchange jacket has heat transferring medium entrance and heat transferring medium outlet.
Rubbish continuous sterilizer the most according to claim 1, it is characterized in that, the outlet of described conveying pipeline is connected with output object temporary storing bin by the first discharge duct, the middle part of described conveying pipeline connects tee T, described tee T has discharge port, and described discharge port is connected with output object temporary storing bin by the second discharge duct.
Rubbish continuous sterilizer the most according to claim 1, it is characterized in that, the exit of described conveying pipeline is provided with medium ball separator, described medium ball separator includes discharge duct, medium ball conveying pipe and output object conveying pipe, described output object conveying pipe connects with described output object temporary storing bin, described medium ball conveying pipe connects with rubbish temporary storing bin, and described medium ball is transported to rubbish temporary storing bin by medium ball conveying pipe.
Rubbish continuous sterilizer the most according to claim 7, it is characterized in that, described medium ball separator also includes separation platform, described discharge duct is vertically arranged, described medium ball conveying pipe may be contained within the lower section of described discharge duct with output object conveying pipe and connects with described discharge duct, described separation platform is positioned at described discharge duct, and described separation platform is inclined relative to horizontal setting and for guiding medium ball to move in medium ball conveying pipe.
Rubbish continuous sterilizer the most according to claim 8, it is characterized in that, described medium ball separator also includes medium ball detector and medium ball flush trimmer, described medium ball detector is arranged at the outside of described discharge duct and for detecting medium ball, described medium ball flush trimmer includes that compressed gas shower nozzle, the outlet of described compressed gas shower nozzle are arranged towards described separation platform.
Rubbish continuous sterilizer the most according to claim 7, it is characterized in that, being provided with the first conveying worm for providing conveying power to medium ball on the pipeline of described medium ball conveying pipe, the entrance and exit of described first conveying worm all connects with described medium ball conveying pipe.
11. rubbish continuous sterilizers according to claim 1, it is characterized in that, the bottom of described rubbish temporary storing bin is provided with the second conveying worm, the entrance of described second conveying worm connects with described rubbish temporary storing bin, and the outlet of described second conveying worm connects with the entrance of described solid pump.
12. 1 kinds of refuse disposal systems, it is characterized in that, including rubbish receiving bin, refuse grinder and rubbish continuous sterilizer as claimed in claim 1, described rubbish receiving bin is connected by the first refuse conveying pipe road with described refuse grinder, described refuse grinder is connected by the second refuse conveying pipe road with described rubbish temporary storing bin, described first refuse conveying pipe road and the second refuse conveying pipe road are the most vertically arranged, and described rubbish receiving bin and described rubbish temporary storing bin lay respectively at above and below described refuse grinder.
13. refuse disposal systems according to claim 12, it is characterized in that, described refuse disposal system also includes device for separation of waste, described device for separation of waste is arranged between described refuse grinder and described rubbish temporary storing bin, described device for separation of waste includes metal delivery tubes, glass delivery tube, for detecting the metal detector of metal, for rejecting the metal removal device of metal and for rejecting the glass flush trimmer of glass, described metal delivery tubes is all obliquely installed with described glass delivery tube and connects with described second refuse conveying pipe road, described metal removal device is arranged at the junction of described metal delivery tubes and described second refuse conveying pipe road, described glass flush trimmer is arranged at the junction of described glass delivery tube and described second refuse conveying pipe road.
14. refuse disposal systems according to claim 13, it is characterised in that described metal delivery tubes connects has metal steriliser, described metal steriliser to include metal sterilization tank and the second heat exchange jacket；Described glass delivery tube road connects has glass steriliser, described glass steriliser to include glass sterilization tank and the 3rd heat exchange jacket.
15. according to the refuse disposal system described in claim 12 or 13, it is characterized in that, described rubbish receiving bin has feeding mouth, is provided with air sparger at described feeding mouth, and described air sparger is for producing the air curtain being isolated from the outside the inside of described rubbish receiving bin.
16. according to the refuse disposal system described in claim 12 or 13, it is characterized in that, being provided with laser bag-breaking device and dispel device in described first refuse conveying pipe road, described laser bag-breaking device has the laser head launching laser beam, described in dispel utensil and have the shower nozzle of jet compression gas.
17. refuse disposal systems according to claim 12, it is characterized in that, the first disinfectant solution ejector and moisture detector it is provided with in described rubbish temporary storing bin, described disinfectant solution ejector electrically connects with moisture detector, and described moisture detector is for detecting the humidity in described rubbish temporary storing bin and sending the control signal of injection disinfectant solution to described disinfectant solution ejector.
18. refuse disposal systems according to claim 16, it is characterised in that be provided with the second disinfectant solution ejector in described rubbish receiving bin and/or described first refuse conveying pipe road.
19. refuse disposal systems according to claim 12, it is characterized in that, described refuse disposal system also includes combustion system, described combustion system includes fine crusher, organic compound combustion device and heat-conducting oil furnace, the outlet of described conveying pipeline is connected with output object temporary storing bin by the first discharge duct, the middle part of described conveying pipeline connects has tee T, described tee T to have discharge port, and described discharge port is connected with output object temporary storing bin by the second discharge duct；The outlet of described output object temporary storing bin connects with described fine crusher, and described fine crusher has the first outlet connected with described organic compound combustion device, and described organic compound combustion device is for heating the heat transferring medium in heat-conducting oil furnace, and described heat-conducting oil furnace connects with described heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620098944.1U CN205460044U (en) | 2016-02-01 | 2016-02-01 | Rubbish continuous sterilization device and system of trash disposal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620098944.1U CN205460044U (en) | 2016-02-01 | 2016-02-01 | Rubbish continuous sterilization device and system of trash disposal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205460044U true CN205460044U (en) | 2016-08-17 |
Family
ID=56672993
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620098944.1U Withdrawn - After Issue CN205460044U (en) | 2016-02-01 | 2016-02-01 | Rubbish continuous sterilization device and system of trash disposal |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205460044U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105688250A (en) * | 2016-02-01 | 2016-06-22 | 李新国 | Waste continuous sterilization device, waste treatment system and waste treatment method |
-
2016
- 2016-02-01 CN CN201620098944.1U patent/CN205460044U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105688250A (en) * | 2016-02-01 | 2016-06-22 | 李新国 | Waste continuous sterilization device, waste treatment system and waste treatment method |
| CN105688250B (en) * | 2016-02-01 | 2018-04-17 | 李新国 | A kind of rubbish continuous sterilizer, refuse disposal system and waste disposal method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2018184384A1 (en) | Comprehensive integrated machine for use in biochemical garbage treatment | |
| US6344638B1 (en) | Method for the disinfection of medical waste in a continuous manner | |
| CN105688250B (en) | A kind of rubbish continuous sterilizer, refuse disposal system and waste disposal method | |
| CN101972769B (en) | Medical rubbish harmless resource comprehensive utilization system | |
| CN206222331U (en) | A kind of domestic garbage disposer | |
| CN103204642A (en) | Novel dry-process cement kiln household garbage incineration method | |
| CN109420657A (en) | A kind of municipal refuse recovery processing integrated apparatus | |
| CN109396161A (en) | The quick volume reduction decrement of crude waste and the method for comprehensive resource processing | |
| CN201105280Y (en) | Medical rubbish high-heat high-pressure wet heat-treating facility | |
| CN206950384U (en) | A kind of larger medical discarded object microwave innocent treatment equipment | |
| CN202212404U (en) | Equipment using municipal solid waste to produce composite dry powder combust for power generation of coal-fired power plants | |
| CN105057307A (en) | Domestic rubbish treatment system | |
| CN107327848A (en) | Mobile garbage handles car | |
| CN107497828A (en) | A kind of clinical waste chemical disinfection harmlessness disposing technique | |
| CN109454088A (en) | A kind of garbage treating process and its system | |
| CN205460044U (en) | Rubbish continuous sterilization device and system of trash disposal | |
| CN206457455U (en) | A kind of carbon black collects granulation packaging system and carbon black production line | |
| CN105444188B (en) | A kind of medical waste microwave handling method and processing equipment | |
| CN107084396A (en) | Environment-friendly type municipal solid wastes directly burn gasification energy supplying system and method for work | |
| CN207013435U (en) | Domestic solid garbage integrated treatment screening installation | |
| CN207049935U (en) | A kind of mobile garbage handles car | |
| CN208448215U (en) | Treatment of!medical waste device | |
| CN206724183U (en) | A kind of environment-friendly type municipal solid wastes directly burn gasification energy supplying system | |
| CN104851469B (en) | Spirally whole bucket feeds processing system to one kind | |
| CN109340757A (en) | A kind of refuse treatment plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160817 Effective date of abandoning: 20180417 |
|
| AV01 | Patent right actively abandoned |