CN214160832U - Solid waste treatment system - Google Patents
Solid waste treatment system Download PDFInfo
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- CN214160832U CN214160832U CN202021654160.5U CN202021654160U CN214160832U CN 214160832 U CN214160832 U CN 214160832U CN 202021654160 U CN202021654160 U CN 202021654160U CN 214160832 U CN214160832 U CN 214160832U
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- 238000009270 solid waste treatment Methods 0.000 title claims abstract description 35
- 239000007789 gas Substances 0.000 claims abstract description 87
- 239000002910 solid waste Substances 0.000 claims abstract description 60
- 238000005336 cracking Methods 0.000 claims abstract description 49
- 238000000197 pyrolysis Methods 0.000 claims abstract description 44
- 239000007788 liquid Substances 0.000 claims abstract description 40
- 239000000428 dust Substances 0.000 claims abstract description 28
- 238000001035 drying Methods 0.000 claims abstract description 9
- 238000011084 recovery Methods 0.000 claims abstract description 9
- 238000000926 separation method Methods 0.000 claims abstract description 9
- 239000002918 waste heat Substances 0.000 claims abstract description 7
- 238000001816 cooling Methods 0.000 claims abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 50
- 230000007246 mechanism Effects 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 3
- 229910001872 inorganic gas Inorganic materials 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims description 2
- 238000002203 pretreatment Methods 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000005406 washing Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 8
- 239000012071 phase Substances 0.000 description 8
- 238000004064 recycling Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000003776 cleavage reaction Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000007017 scission Effects 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007792 gaseous phase Substances 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 239000002906 medical waste Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000008234 soft water Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Gasification And Melting Of Waste (AREA)
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a solid waste treatment system, which comprises a dryer, a cracking reactor and a cracking product treatment system, wherein the dryer is used for drying solid waste; the cracking reactor is connected with the dryer and is used for carrying out anaerobic cracking treatment on the dried solid waste to generate solid waste residue and cracking gas; the pyrolysis product treatment system comprises a solid waste residue recovery unit and a gas phase treatment unit which are connected with the pyrolysis reactor; the gas phase treatment unit comprises a dust remover, a condenser and a gas-liquid separator; the dust remover is connected with the cracking reactor and is used for removing dust from the cracking gas; the dust remover is connected with the dryer so as to recycle the waste heat of the cracked gas after dust removal to the dryer, and the condenser is connected with the dryer and used for cooling the cracked gas after being utilized by the dryer; the gas-liquid separator is connected with the condenser and the dryer and is used for performing gas-liquid separation on the cooled pyrolysis gas and the pyrolysis gas utilized by the dryer. The solid waste treatment system can realize solid waste reduction, reduce pollution and save energy consumption.
Description
Technical Field
The utility model belongs to the technical field of solid waste handles technique and specifically relates to a solid waste processing system is related to.
Background
The organic solid waste is waste which is inevitably generated in production and life and has huge yield, such as meal waste, kitchen waste, medical waste, organic sludge and the like. With the continuous acceleration of urban modernization process, the emission of primary solid wastes is increased day by day. The existing treatment methods for organic solid wastes mainly comprise sanitary landfill, incineration and the like. Wherein, because the quantity of the organic solid waste is huge, the land occupation quantity of the sanitary landfill is large, and the land is permanently occupied irreparably, the secondary pollution generated by the landfill is serious, and the odor is scattered; the incineration method has great difficulty in treating tail gas, thereby causing atmospheric pollution. Therefore, the traditional organic solid waste treatment method can cause serious land and air pollution at present, and is difficult to adapt to the requirement of sustainable development.
SUMMERY OF THE UTILITY MODEL
The utility model discloses aim at solving one of the technical problem that exists among the prior art at least. Therefore, the utility model provides a solid waste processing system.
In a first aspect, an embodiment of the present invention provides a solid waste treatment system, including:
the dryer is used for drying the solid waste;
the cracking reactor is connected with the dryer and is used for receiving the solid waste treated by the dryer and carrying out anaerobic cracking treatment on the solid waste to generate solid waste residues and cracking gas;
the pyrolysis product treatment system comprises a solid waste residue recovery unit and a gas phase treatment unit which are connected with the pyrolysis reactor; the gas phase treatment unit comprises a dust remover, a condenser and a gas-liquid separator; the dust remover is connected with the cracking reactor and is used for removing dust from the cracking gas; the dust remover is also connected with the dryer so as to recycle the waste heat of the cracked gas after dust removal treatment to the dryer for drying treatment, and the condenser is connected with the dryer and is used for cooling the cracked gas after being utilized by the dryer; the gas-liquid separator is respectively connected with the condenser and the dryer and is used for carrying out gas-liquid separation treatment on the pyrolysis gas treated by the condenser and the pyrolysis gas utilized by the dryer.
The utility model discloses solid waste processing system has following beneficial effect at least: the solid waste treatment system adopts the arrangement of the dryer and the cracking reactor, and can remove moisture in the solid waste and carry out high-temperature cracking treatment on organic matters in the solid waste so as to reduce the solid waste; by arranging the gas phase treatment unit, the pyrolysis gas generated after the treatment of the pyrolysis reactor can be subjected to dust removal purification and gas-liquid separation treatment, so that the treated gas is suitable for recycling or combustion emission, and the atmospheric pollution is reduced; and the waste heat of the cracked gas after dust removal treatment can be reused in the dryer, so that the resource recycling can be realized, and the energy consumption is saved.
According to other embodiments of the present invention, the pyrolysis reactor is connected to the dryer through the air shutoff machine.
According to other embodiments of the present invention, the gas phase processing unit further comprises a gas washing device, the gas washing device is connected to the gas-liquid separator, and is used for treating the gas separated by the gas-liquid separator to remove inorganic gas components.
According to further embodiments of the present invention, the solid waste treatment system further comprises a first steam generator and a superheater; the first steam generator is connected with the superheater and used for generating steam to be supplied to the superheater; the superheater is connected with the cracking reactor and used for converting the steam provided by the first steam generator into superheated steam and supplying the superheated steam to the cracking reactor.
According to other embodiments of the present invention, the first steam generator is a gas steam generator, and the first steam generator is further connected to the gas-liquid separator for receiving and combusting the gas separated by the gas-liquid separator to generate steam for supplying the steam to the superheater;
or, the solid waste treatment system further comprises a second steam generator, the second steam generator is a gas steam generator, and the second steam generator is respectively connected with the gas-liquid separator and the superheater and is used for receiving and combusting the gas separated by the gas-liquid separator to generate steam to be supplied to the superheater.
According to other embodiments of the present invention, the solid waste treatment system further comprises a water inlet pretreatment system, the water inlet pretreatment system is connected to the first steam generator, and the water inlet pretreatment system is used for pre-softening and filtering the water inlet of the first steam generator.
According to other embodiments of the present invention, the solid waste treatment system further comprises a feeding mechanism, the feeding mechanism is connected with the dryer, and is used for conveying the solid waste to the dryer.
According to the utility model discloses a further embodiment, solid waste processing system still includes the pretreatment system, the pretreatment system with feeding mechanism connects, be used for to carry out earlier breakage and squeeze dewatering treatment to solid waste before the feeding mechanism feed.
According to other embodiments of the present invention, the solid waste recovery unit comprises a screw discharger and a receiving barrel, one end of the screw discharger is connected to the pyrolysis reactor, and a discharge valve is disposed between the screw discharger and the pyrolysis reactor; the material receiving barrel is arranged at the other end of the spiral unloading machine and used for collecting and unloading materials.
According to other embodiments of the present invention, the solid waste treatment system further comprises a water circulation system, the water circulation system comprising a circulation water tank and a circulation water pump; the cracking reactor and the condenser are respectively connected with the circulating water tank so as to discharge water generated by the cracking reactor and the condenser to the circulating water tank; the circulating water tank is respectively connected with the cracking reactor and the condenser through the circulating water pump so as to be used for respectively pumping water in the circulating water tank back to the cracking reactor and the condenser.
Drawings
FIG. 1 is a schematic view of a solid waste treatment system according to an embodiment of the present invention.
Detailed Description
The conception and the resulting technical effects of the present invention will be described clearly and completely with reference to the following embodiments, so that the objects, features and effects of the present invention can be fully understood. Obviously, the described embodiments are only a part of the embodiments of the present invention, and not all embodiments, and other embodiments obtained by those skilled in the art without inventive labor based on the embodiments of the present invention all belong to the protection scope of the present invention.
In the description of the embodiments of the present invention, if an orientation description is referred to, for example, the directions or positional relationships indicated by "upper", "lower", "front", "rear", "left", "right", etc. are based on the directions or positional relationships shown in the drawings, only for convenience of description and simplification of description, but not for indicating or implying that the indicated device or element must have a specific orientation, be constructed and operated in a specific orientation, and thus should not be construed as limiting the present invention.
In the description of the embodiments of the present invention, if a feature is referred to as being "disposed", "fixed", "connected", or "mounted" on another feature, it can be directly disposed, fixed, or connected to the other feature or indirectly disposed, fixed, connected, or mounted on the other feature. In the description of the embodiments of the present invention, if "a plurality" is referred to, it means one or more, if "a plurality" is referred to, it means two or more, if "greater than", "less than" or "more than" is referred to, it is understood that the number is not included, and if "more than", "less than" or "within" is referred to, it is understood that the number is included. If reference is made to "first" or "second", this should be understood to distinguish between features and not to indicate or imply relative importance or to implicitly indicate the number of indicated features or to implicitly indicate the precedence of the indicated features.
Referring to fig. 1, fig. 1 is a schematic structural diagram of an embodiment of the solid waste treatment system of the present invention. As shown in fig. 1, the solid waste treatment system includes a dryer 10, a cleavage reactor 20, and a cleavage product treatment system. The dryer 10 is used for drying solid waste. The cracking reactor 20 is connected to the dryer 10, and is configured to receive the solid waste processed by the dryer 10 and perform anaerobic cracking treatment on the solid waste to generate solid waste residues and cracking gas. The pyrolysis product treatment system comprises a solid waste residue recovery unit and a gas phase treatment unit which are connected with the pyrolysis reactor 20; the gas phase treatment unit includes a dust collector 41, a condenser 42, and a gas-liquid separator 43; the dust collector 41 is connected with the cracking reactor 20 and is used for dedusting the cracked gas, and the dust collector 41 can specifically adopt a cyclone dust collector, an electrostatic dust collector, a filter dust collector and the like; the dust remover 41 is also connected with the dryer 10 so as to recycle the waste heat of the treated pyrolysis gas to the dryer 10 for drying treatment; the condenser is connected with the dryer and is used for cooling the pyrolysis gas utilized by the dryer 10; the gas-liquid separator 43 is connected to the condenser 42 and the dryer 10, and is configured to perform gas-liquid separation on the pyrolysis gas processed by the condenser 42 and the pyrolysis gas used by the dryer 10.
When the solid waste treatment system is used, the solid waste is dried by the dryer 10 to remove moisture, and then is introduced into the cracking reactor 20 to be cracked at high temperature under an anaerobic condition, so that the organic solid waste is cracked to generate solid waste residues and cracked gas, wherein the solid waste residues are collected and recovered by the solid waste residue recovery unit, and can be specifically selected as fuel and fertilizer according to different components of the solid waste residues, and the solid waste can be buried and the like; the pyrolysis gas is introduced into a dust collector 41 in the gas phase processing unit for dust removal processing, and the processed pyrolysis gas has a large amount of waste heat and can be recycled to the dryer 10, so that the pyrolysis gas is introduced into the dryer 10, and further, according to the specific situation of the pyrolysis gas after drying processing, the pyrolysis gas is introduced into a condenser 42 for cooling and then introduced into a gas-liquid separator 43 for gas-liquid separation processing, or is directly subjected to gas-liquid separation processing through the gas-liquid separator 43. The water produced after gas-liquid separation can be reused, and the treated gas is suitable for recycling or combustion discharge, so that the atmospheric pollution can be reduced.
In order to facilitate feeding of the solid waste, the solid waste treatment system of this embodiment further includes a feeding mechanism 50, the feeding mechanism 50 is connected to the dryer 10 and is configured to convey the solid waste to the dryer 10, and the feeding mechanism 50 is specifically a screw conveyor, but in other embodiments, other feeding mechanisms may be adopted.
In order to improve the subsequent treatment efficiency of the solid waste, the solid waste treatment system may further include a pretreatment system 60, and the pretreatment system 60 is connected to the feeding mechanism 50 and is configured to crush and squeeze the solid waste to remove water before feeding the solid waste to the feeding mechanism 50. In this embodiment, the pretreatment system 60 employs a crushing and squeezing integrated machine to crush and squeeze the solid waste to remove water, so as to facilitate the subsequent cracking and carbonization of organic matters in the cracking reactor 20 and the drying and reduction of solid residues.
In order to facilitate the formation of the anaerobic condition of the cracking reactor 20 during the treatment process, so as to facilitate the proceeding of the anaerobic cracking reaction and improve the treatment efficiency, in this embodiment, the cracking reactor 20 is connected with the dryer 10 by a wind-off fan. Because in the processing procedure, pyrolysis reactor 20 utilizes high temperature superheated steam to promote the organic matter schizolysis, so need isolated oxygen, and through the setting of closing the fan, can play the effect of similar valve, control solid waste from the desicator gets into for intermittent type formula feeding in pyrolysis reactor 20, specifically send into a definite material in pyrolysis reactor 20 after, close the fan, the minute quantity oxygen that gets into in pyrolysis reactor 20 can be taken away to steam to keep the anaerobic cracking state in pyrolysis reactor 20.
In order to further make the finally discharged gas meet the discharge standard and reduce pollution, the gas phase treatment unit in the solid waste treatment system may further include a gas washing device 44, and the gas washing device 44 is connected to the gas-liquid separator 43 and is used for treating the gas separated by the gas-liquid separator 43 to remove inorganic gas components therein. The gas washing mode of the gas washing device 44 can be acid washing, alkaline and the like, and particularly, the corresponding gas washing device can be selected according to the gas condition generated by the anaerobic cracking of the solid waste in the actual treatment.
The solid waste treatment system of the embodiment further comprises a first steam generator 71 and a superheater 72, wherein the first steam generator 71 is connected with the superheater 72 and is used for generating steam to be supplied to the superheater 72; the superheater 72 is connected to the cracking reactor 20, and converts the steam supplied from the first steam generator 71 into superheated steam, which is supplied to the cracking reactor 20. Of course, in other embodiments, the first steam generator 71 and the superheater 72 may not be included, and when in use, the first steam generator and the superheater are used in cooperation with the external first steam generator and the superheater.
In addition, the solid waste treatment system of the embodiment further includes a second steam generator 73, the second steam generator 73 is a gas steam generator, and the second steam generator 73 is respectively connected to the gas-liquid separator 43 and the superheater 72, and is configured to receive and combust the gas separated by the gas-liquid separator 43 to generate steam for supplying to the superheater 72. The second steam generator 73 is usually provided with a water tank 731, and by the arrangement of the second steam generator 73, comprehensive utilization of resources can be realized, and energy consumption for treatment can be reduced.
The gas-liquid separator 43 may be connected to the second steam generator 73 by a first induced draft fan 74; in order to ensure sufficient gas required by the second steam generator 73 and confirm the normal operation of the system, a gas supply system may be additionally provided to supply gas to the second steam generator 73, and the gas supply system may include a gas storage tank 75 and a vaporizing furnace 76, and the gas storage tank 75, the vaporizing furnace 76 and the second steam generator 73 are connected in sequence. The second steam generator 73 is further provided with an exhaust port 732 and can be further connected with the gas washing device 44 through the second induced draft fan 77, and in the using process, the gas separated by the gas-liquid separator 43 can be directly discharged through the exhaust port 732 or discharged after being processed by the gas washing device 44 according to the condition that the gas is generated after being combusted in the second steam generator 73.
Of course, in other embodiments, the second steam generator 73 may be eliminated, and the first steam generator 71 is specifically a gas steam generator, and the first steam generator 71 is further connected to the gas-liquid separator 43 for receiving and combusting the gas separated by the gas-liquid separator 43 to generate steam for supplying to the superheater 72.
In order to improve the quality of the used water and reduce the influence of the used water on the equipment, the solid waste treatment system may further include a water inlet pretreatment system 80, and the water inlet pretreatment system 80 is connected to the first steam generator 71 and is used for performing softening filtration treatment on the water inlet of the first steam generator 71 in advance. The influent water pretreatment system 80 may specifically employ a soft water filter.
In order to further improve the recycling rate and reduce the resource energy consumption, the solid waste treatment system may further include a water circulation system, the water circulation system may specifically include a circulation water tank 91 and a circulation water pump 92, the pyrolysis reactor 20 and the condenser 42 are respectively connected to the circulation water tank 91 to discharge water generated by the pyrolysis reactor 20 and the condenser 42 to the circulation water tank 91, and the circulation water tank 91 is respectively connected to the pyrolysis reactor 20 and the condenser 42 through the circulation water pump 92 to pump the storage water in the circulation water tank 91 for recycling to the pyrolysis reactor 20 and the condenser 42, so as to recycle the water in the circulation water tank 91.
In addition, in this embodiment, the solid waste recovery unit includes a screw discharger 31 and a receiving barrel 32, one end of the screw discharger 31 is connected to the cracking reactor 20, and a discharge valve 33 is disposed between the screw discharger 31 and the cracking reactor 20; the receiving barrel 32 is arranged at the other end of the screw discharger 31 and is used for collecting and discharging materials. Of course, in other embodiments, the solid waste recovery unit may directly employ a receiving container to collect the solid waste generated by the anaerobic cracking process in the cracking reactor 20.
In the above solid waste treatment system, the connection between the devices for gas (or vapor) and liquid transportation generally adopts a pipeline connection, and a control valve may be provided on the pipeline for the convenience of controlling the circulation.
By the above, the utility model discloses adopt the setting of desicator 10 and pyrolysis reactor 20 among the solid waste processing system, can get rid of the moisture among the solid waste and carry out pyrolysis treatment to its wherein organic matter to realize the minimizing of solid waste, and through the setting of gaseous phase processing unit, can carry out dust removal purification, gas-liquid separation to the pyrolysis gas that produces after the pyrolysis reactor 20 handles and handle, so that the gas is suitable for recycle or burning discharge after handling, reduces the atmospheric pollution; and the waste heat of the cracked gas after dust removal can be reused in the dryer 10, so that the resource recycling can be realized, and the energy consumption is saved.
The embodiments of the present invention have been described in detail with reference to the accompanying drawings, but the present invention is not limited to the above embodiments, and various changes can be made without departing from the spirit of the present invention within the knowledge of those skilled in the art. Furthermore, the embodiments of the present invention and features of the embodiments may be combined with each other without conflict.
Claims (10)
1. A solid waste treatment system, comprising:
the dryer is used for drying the solid waste;
the cracking reactor is connected with the dryer and is used for receiving the solid waste treated by the dryer and carrying out anaerobic cracking treatment on the solid waste to generate solid waste residues and cracking gas;
the pyrolysis product treatment system comprises a solid waste residue recovery unit and a gas phase treatment unit which are connected with the pyrolysis reactor; the gas phase treatment unit comprises a dust remover, a condenser and a gas-liquid separator; the dust remover is connected with the cracking reactor and is used for removing dust from the cracking gas; the dust remover is also connected with the dryer so as to recycle the waste heat of the cracked gas after dust removal treatment to the dryer for drying treatment, and the condenser is connected with the dryer and is used for cooling the cracked gas after being utilized by the dryer; the gas-liquid separator is respectively connected with the condenser and the dryer and is used for carrying out gas-liquid separation treatment on the pyrolysis gas treated by the condenser and the pyrolysis gas utilized by the dryer.
2. The solid waste treatment system of claim 1, wherein the pyrolysis reactor is connected to the dryer by an airlock.
3. The solid waste treatment system of claim 1, wherein the gas phase treatment unit further comprises a gas scrubber connected to the gas-liquid separator for processing the gas separated by the gas-liquid separator to remove inorganic gas components.
4. The solid waste treatment system of claim 1, further comprising a first steam generator and a superheater; the first steam generator is connected with the superheater and used for generating steam to be supplied to the superheater; the superheater is connected with the cracking reactor and used for converting the steam provided by the first steam generator into superheated steam and supplying the superheated steam to the cracking reactor.
5. The solid waste treatment system of claim 4, wherein the first steam generator is a gas steam generator, the first steam generator further coupled to the gas-liquid separator for receiving and combusting the separated gas from the gas-liquid separator to generate steam for supplying the superheater;
or, the solid waste treatment system further comprises a second steam generator, the second steam generator is a gas steam generator, and the second steam generator is respectively connected with the gas-liquid separator and the superheater and is used for receiving and combusting the gas separated by the gas-liquid separator to generate steam to be supplied to the superheater.
6. The solid waste treatment system of claim 4, further comprising a influent pretreatment system coupled to the first steam generator for pre-softening and filtering influent water from the first steam generator.
7. The solid waste treatment system of claim 1, further comprising a feed mechanism coupled to the dryer for conveying solid waste to the dryer.
8. The solid waste treatment system of claim 7, further comprising a pre-treatment system connected to the feeding mechanism for crushing and pressing the solid waste to remove water before feeding the solid waste to the feeding mechanism.
9. The solid waste treatment system of any one of claims 1 to 8, wherein the solid waste recovery unit comprises a screw discharger and a receiving bucket, one end of the screw discharger is connected with the pyrolysis reactor, and a discharge valve is arranged between the screw discharger and the pyrolysis reactor; the material receiving barrel is arranged at the other end of the spiral unloading machine and used for collecting and unloading materials.
10. The solid waste treatment system of any one of claims 1 to 8, further comprising a water circulation system including a circulation water tank and a circulation water pump; the cracking reactor and the condenser are respectively connected with the circulating water tank so as to discharge water generated by the cracking reactor and the condenser to the circulating water tank; the circulating water tank is respectively connected with the cracking reactor and the condenser through the circulating water pump so as to be used for respectively pumping water in the circulating water tank back to the cracking reactor and the condenser.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021654160.5U CN214160832U (en) | 2020-08-10 | 2020-08-10 | Solid waste treatment system |
| PCT/CN2020/116099 WO2022032801A1 (en) | 2020-08-10 | 2020-09-18 | Solid waste treatment system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021654160.5U CN214160832U (en) | 2020-08-10 | 2020-08-10 | Solid waste treatment system |
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| CN214160832U true CN214160832U (en) | 2021-09-10 |
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| WO (1) | WO2022032801A1 (en) |
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| CN115044622A (en) * | 2022-07-18 | 2022-09-13 | 滦南林海科技发展有限责任公司 | Comprehensive utilization method of industrial organic solid waste |
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| CN1095701C (en) * | 1999-08-05 | 2002-12-11 | 杨剑 | Process for treating combustible garbage |
| CN100422119C (en) * | 2003-11-05 | 2008-10-01 | 叶山控股有限公司 | Organic refuse piling-free processing system and method |
| CN101693251B (en) * | 2009-10-23 | 2011-11-09 | 中国海洋石油总公司 | Thermal cracking resource processing technology of domestic refuse in marine ships |
| TW201332672A (en) * | 2012-02-07 | 2013-08-16 | Zhuang Rong | Waste recycling method and device thereof |
| EP2679659B1 (en) * | 2012-06-29 | 2016-08-24 | Global Gateways Lux HoldCo S.A. | Method and plant for production of a fuel gas from waste |
| CN203664336U (en) * | 2013-11-11 | 2014-06-25 | 张艺璇 | Resource self-consumption type waste treatment system for white waste |
| CN206139634U (en) * | 2016-10-28 | 2017-05-03 | 深圳华云环保科技发展有限公司 | House refuse disposal system |
| CN107626726A (en) * | 2017-11-03 | 2018-01-26 | 董平年 | A kind of cracking reduction conversion reaction handling process of life debirs |
| CN208019124U (en) * | 2018-01-06 | 2018-10-30 | 修武永乐新能源环保设备有限公司 | A kind of system of cement kiln cooperative disposal domestic waste |
| CN109530409A (en) * | 2018-12-25 | 2019-03-29 | 周新 | The system and method for class organic compound is synthesized in a kind of processing house refuse |
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