CN201795494U - Refuse pyrolysis produced gas treatment device - Google Patents
Refuse pyrolysis produced gas treatment device Download PDFInfo
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- CN201795494U CN201795494U CN201020533308XU CN201020533308U CN201795494U CN 201795494 U CN201795494 U CN 201795494U CN 201020533308X U CN201020533308X U CN 201020533308XU CN 201020533308 U CN201020533308 U CN 201020533308U CN 201795494 U CN201795494 U CN 201795494U
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- 238000001035 drying Methods 0.000 claims abstract description 39
- 239000000428 dust Substances 0.000 claims abstract description 16
- 239000007789 gas Substances 0.000 claims abstract description 12
- 238000007873 sieving Methods 0.000 claims abstract description 11
- 239000000779 smoke Substances 0.000 claims abstract description 11
- 238000011084 recovery Methods 0.000 claims abstract description 9
- 239000010813 municipal solid waste Substances 0.000 claims description 105
- 239000002918 waste heat Substances 0.000 claims description 21
- 239000007787 solid Substances 0.000 claims description 9
- 238000007599 discharging Methods 0.000 claims description 8
- 239000002893 slag Substances 0.000 claims description 8
- 238000009434 installation Methods 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- 239000011819 refractory material Substances 0.000 claims description 6
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- 229920006395 saturated elastomer Polymers 0.000 claims description 3
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- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract 1
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Abstract
The utility model provides a refuse pyrolysis produced gas treatment device, which is formed by sequentially connecting a refuse treatment device, a refuse drying device, a refuse pyrolysis device, an afterheat recovery and utilization device and a smoke gas purifier. The utility model is characterized in that the refuse treatment device comprises a refuse material bin (1), a material feeding machine (2), a refuse conveyer (3), refuse sieving equipment (4) and a refuse crushing machine (5), wherein the refuse drying device comprises a refuse drying machine (6), the refuse pyrolysis device comprises a pyrolysis drum (7), a cyclone dust collector (8), a pyrolysis gas burner (9) and an indirect cooler (10), the afterheat recovery and utilization device comprises a afterheat boiler (11) and a steam power generator set (12), and the smoke gas purifier comprises a cloth bag dust remover (13). The refuse enters the pyrolysis drum after being treated, organic matters in the refuse are converted into energy sources after the pyrolysis under the air isolation condition, and inorganic matters are completed mineralized to become refuse carbon. The utility model solves the refuse treatment problem, realizes the stable production, and avoids the secondary pollution such as dioxin and the like, in addition, both the produced fuel gas and the refuse carbon are valuable substances, the effect of no waste generation in the whole process can be realized, and the clean production can be completely realized.
Description
Technical field
The utility model belongs to the domestic rubbish disposal technical field, is specifically related to a kind of refuse pyrolysis aerogenesis disposal plant.
Background technology
The energy and environment are two big principal elements of restriction human survival and development.Particularly entered since the modernized society, large-scale production with consumption produces a large amount of discarded objects, simultaneously, the fast development that urbanization is built, the municipal refuse problem is on the rise, and not only component of refuse is increasingly sophisticated, and quantity sharply increases.At present the rubbish output in whole world every year has caused the extensive concern of countries in the world up to 10,000,000,000 tons of problem of environmental pollutions that rubbish caused.No matter be developed country or developing country, all realized the inconvenience that garbage problem brings to the human lives deeply.
Rubbish is inevitable product among the human lives, the human puzzlement that can not avoid because of rubbish brought.Rubbish is in its collection, transportation and processing procedure, and himself and the harmful components that produce have all caused pollution to environment such as atmosphere, soil, water bodys.It is soaring not have plan landfill place stench, and mouse, fly etc. multiplies breeding, and communicate illness becomes the persistent ailment of urban environment and the root of environmental pollution.In a single day the natural environment that the mankind depend on for existence is corrupted to the degree that is difficult to recover, and human existence will be subjected to stern challenge, even may reach limit.Therefore garbage disposal has become the environmental problem that enjoys the world to attract attention.Many knowledgeable people just propose in eighties of last century, and the innoxious process for treating of domestic waste is the protection environment, improve ecologically, prevent and remedy pollution and promote economy and ecological environment to reach one of important content of sustainable development.The energy and the environmental problem in the processing of domestic waste and utilization and the whole world are closely bound up, if the garbage problem in city can not well solve, certainly will have a strong impact on advancing of human society.How to reduce the discharge capacity of rubbish, realize innoxious, minimizing, the resource of rubbish, the turn waste into wealth resource that realizes rubbish of rubbish is recycling, be an important topic in the management of China's garbage disposal and modern city.
Landfill method commonly used in the prior art, composting process and burning method, said method is all given new pollution of environment and infringement undoubtedly, it is the innoxious of municipal refuse that municipal refuse adopts the pyrolysis carbonization, the effective way of minimizing and resource, realize the real utilization rate of heat value that needs to consider rubbish of promoting, the processing and the utilization of the removal of harmful substance and pyrolysis venting body, Chinese invention patent application such as CN101101121(were on 01 09th, 2008 in open day) a kind of domestic garbage pyrolysis gasification oven is provided, comprise and add feed bin, body of heater, add feed bin and be located at body of heater inlet top, on the feed entrance of body of heater, be provided with the horizontal movable type water sealing device, be provided with the flip-shell water sealing device adding on the reinforced inlet of feed bin, the bottom that adds feed bin is made up of panel turnover component, is provided with closed cover in the horizontal movable type water sealing device periphery of discharging opening that adds feed bin and body of heater inlet.This pyrolysis oven pyrolytic gasification is effective, gas output is high, charging is smooth and easy, garbage disposal efficient height, the domestic transformation that also has more manufacturer to be devoted to pyrolysis oven, fail to form from the pyrolysis pre-treatment to pyrolysis after the whole system research of waste heat recovery.
Summary of the invention
The utility model is for solving prior art the problems referred to above, provide a kind of simple in structure, stability good, handle cost-effective refuse pyrolysis aerogenesis disposal plant, the organic principle of discarded object is converted into energy in the refuse pyrolysis process, has better economic; The secondary pollution of pyrolysis system is little, and environment is safer.Pyrolysis is carried out under the condition of anaerobic or anoxic, reduces the generation of bioxin.The solid product of pyrolysis is a garbage carbon, can be used as chemical industry or building materials raw material after the decomposition respectively and uses and other industrial circles, realizes decrement discharge, harmless processing, can realize complete cleaner production.
For realizing the utility model purpose, adopt following technical scheme:
A kind of refuse pyrolysis aerogenesis disposal plant, by refuse disposal installation, the drying garbage device, refuse pyrolysis plant, heat recovery device and smoke eliminator connect successively, it is characterized in that refuse disposal installation comprises the rubbish feed bin, batcher, garbage conveyor, sieving garbage equipment and refuse grinder, the drying garbage device comprises rubbish drying machine, refuse pyrolysis plant comprises the pyrolysis drum, cyclone dust collectors, pyrolysis air burner and indirect cooler, the heat recovery device comprises waste heat boiler and steam-electric power unit, smoke eliminator comprises sack cleaner, rubbish in the rubbish feed bin is sent into sieving garbage equipment by batcher and garbage conveyor, sieving garbage equipment connects rubbish drying machine and refuse grinder, rubbish drying machine and refuse grinder connect the refuse pyrolysis drum, the refuse pyrolysis drum is provided with the charging ship lock, the pyrolysis chamber, the discharging ship lock, the pyrolysis of discharging in order to inlet plenum that the thermal decomposition thermal source is provided and discharge chamber and solid residue bloats the slag device, refuse pyrolysis bloats mouth and connects cyclone dust collectors, the cyclone dust collectors outlet connects the pyrolysis air burner, the outlet of pyrolysis air burner is communicated with the inlet plenum and the waste heat boiler of refuse pyrolysis drum, waste heat boiler connects the steam-electric power unit, the tail gas outlet of waste heat boiler connects sack cleaner, and sack cleaner connects chimney.
The utility model processing procedure is: handled rubbish is introduced into the rubbish feed bin, sending into screening plant by batcher and garbage conveyor sieves, the higher rubbish drying machine that enters of fine grained msw water content carries out drying, and coarse granule rubbish together enters refuse pyrolysis drum with dried rubbish after by refuse grinder.Refuse pyrolysis bloats mouth and is provided with cyclone dust collectors, after the dedusting of pyrolysis gas, enters the burning of pyrolysis air burner via cyclone dust collectors, and the hot flue gas part of generation enters the refuse pyrolysis drum, for pyrolysis provides heat.The hot flue gas of another part enters waste heat boiler and produces steam, generates electricity via the steam-electric power unit, after tail gas enters sack cleaner dedusting, desulfurization, through smoke stack emission.The utility model will pass through the screening plant sorting earlier from the rubbish of rubbish feed bin, the higher rubbish drying machine that enters of fine grained msw water content carries out drying, coarse granule rubbish together enters refuse pyrolysis drum with dried rubbish after by refuse grinder, pyrolysis under the condition of secluding air in drum, organic matter in the rubbish changes into fuel gas, the inorganic matter permineralization becomes garbage carbon.Hot flue gas enters waste heat boiler, produces steam and generates electricity via the steam-electric power unit, and the steam that leaves generating set is got back to rubbish drying machine provides energy for drying garbage.
Rubbish drying machine is the indirect swinging drying drum that has the twice tube bank, and the heat transferring medium in the pipeline is the saturated vapor that waste heat boiler produces, and there is certain angle of inclination in the rotating cylinder of rubbish drying machine.Rubbish contacts the back and absorbs energy with heat exchanger tube, moisture contained in the rubbish is evaporated.Because the effect of the inclination angle of drying machine, rubbish is sent to discharge chamber from the porch.
A rotary barrel is drawn together in the pyrolysis bulge, cylindrical shell is outer to be rolled into a hollow chamber by refractory material, conduct heat in the chamber that the high-temperature flue gas that comes out from the combustion chamber forms as heating carrier between refractory material and rotary barrel, the pyrolysis drum refuse pyrolysis, produces pyrolysis gas and solid residue at starvation and when absorbing heat of high temperature.Rubbish does not burn because of anaerobic in this course, thus seldom produce bioxin, and produce less dust, and the fine grained heavy metal is cured in the solid residue, and the reguline metal is separated from solid residue again and is utilized.
Described pyrolysis bloats the slag device and connects cold indirect cooler.After solid residue enters cooling device and cools off, discharge by conveying screw rod.
Between drying garbage device and the refuse pyrolysis plant, the Solid Conveying and Melting that bloats between slag device and the cooling device of pyrolysis is screw feeder or conveyer belt feed.
Compared to existing technology, the utility model beneficial effect is that the organic principle of discarded object is converted into energy in the refuse pyrolysis process, has better economic; The secondary pollution of pyrolysis system is little, and environment is safer.Pyrolysis is carried out under the condition of anaerobic or anoxic, avoids the generation of bioxin.The solid product of pyrolysis is a garbage carbon, can be used as chemical industry or building materials raw material after the decomposition respectively and uses and other industrial circles, realizes decrement discharge, harmless processing, thereby has reached the purpose of environmental protection and cleaner production perfect adaptation.
Description of drawings
Accompanying drawing 1 is the structural representation of the utility model refuse pyrolysis aerogenesis disposal plant.
Among the figure, 1 is the rubbish feed bin, and 2 is batcher, 3 is garbage conveyor, and 4 is sieving garbage equipment, and 5 is refuse grinder, 6 is rubbish drying machine, and 7 are the pyrolysis drum, and 8 is cyclone dust collectors, 9 are the pyrolysis air burner, 10 indirect coolers, 11 is waste heat boiler, 12 are the steam-electric power unit, 13 is sack cleaner, and 14 is chimney.
The specific embodiment
Below in conjunction with accompanying drawing the specific embodiment of the present utility model is described in further detail:
Embodiment 1:
Referring to Fig. 1, a kind of refuse pyrolysis aerogenesis disposal plant of the present utility model is connected successively by refuse disposal installation, drying garbage device, refuse pyrolysis plant, heat recovery device and smoke eliminator,
Comprise rubbish feed bin 1, batcher 2, garbage conveyor 3, sieving garbage equipment 4, refuse grinder 5, rubbish drying machine 6, pyrolysis drum 7, cyclone dust collectors 8, pyrolysis air burner 9, indirect cooler 10, waste heat boiler 11, steam-electric power unit 12, sack cleaner 13 and chimney 14.
Rubbish feed bin 1, batcher 2, garbage conveyor 3, sieving garbage equipment 4 and refuse grinder 5 are refuse disposal installation, the drying garbage device comprises rubbish drying machine 6, pyrolysis drum 7, cyclone dust collectors 8, pyrolysis air burner 9 and indirect cooler 10 are refuse pyrolysis plant, waste heat boiler 11 and steam-electric power unit 12 are the heat recovery device, and smoke eliminator comprises sack cleaner 13.
Refuse disposal installation is to the screening of rubbish and break process, earlier rubbish is sieved, and the bulky grain that screening obtains enters refuse grinder 5 again and is broken into the fine grained that meets the demands.
Rubbish drying machine 6 is for having the indirect swinging drying drum of twice tube bank, and the heat transferring medium in the pipeline is the saturated vapor that waste heat boiler 11 produces, and rubbish contacts the back and absorbs energy with heat exchanger tube, and moisture contained in the rubbish is evaporated.There is certain angle of inclination in the rotating cylinder of rubbish drying machine.Because the effect of the inclination angle of rubbish drying machine, rubbish is sent to discharge chamber from the porch.
The tail gas outlet of waste heat boiler connects sack cleaner 13, and the outlet of deduster 13 connects chimney 14.
Pyrolysis bloats slag system, and the rubbish charcoal enters indirect cooler 10.
The pyrolysis bulge is drawn together rotating furnace body, is used to support the also support and the smoke chamber of rotating furnace that body of heater is cylindric, is provided with some grades pyrolysis cylindrical shell in it, is provided with turbulent muscle in the pyrolysis cylindrical shell, is the smoke chamber around the pyrolysis cylindrical shell between the cylindrical shell of pyrolysis oven and the body of heater.
Pyrolysis drum 7 comprises a rotary barrel, and cylindrical shell is outer to be rolled into a hollow chamber by refractory material, heats in the chamber that the high-temperature flue gas that comes out from combustion chamber 9 forms between refractory material and rotary barrel as heating carrier.Rubbish is heated in rotary drum, and the pyrolysis chemical reaction takes place.
The course of work is as follows:
Rubbish in the rubbish feed bin 1 is sent into sieving garbage equipment 4 by batcher 2 and garbage conveyor 3, fine grained rubbish that sorting obtains and coarse granule rubbish, the higher rubbish drying machine 6 that enters of fine grained msw water content carries out drying, coarse granule rubbish together enters refuse pyrolysis drum 7 by refuse grinder 5 backs with dried rubbish, refuse pyrolysis drum 7 is provided with the charging ship lock, the pyrolysis chamber, the discharging ship lock, the pyrolysis of discharging in order to inlet plenum that the thermal decomposition thermal source is provided and discharge chamber and solid residue bloats the slag device
7 outlets of refuse pyrolysis drum connect cyclone dust collectors 8, cyclone dust collectors 8 outlets connect pyrolysis air burner 9, the outlet of pyrolysis air burner 9 is communicated with the inlet plenum and the waste heat boiler 11 of refuse pyrolysis drum 7, waste heat boiler 11 connects steam-electric power unit 12, the tail gas outlet of waste heat boiler 11 connects sack cleaner 13, and sack cleaner 13 connects chimney 14.
Inorganic matter permineralization in the rubbish is transformed into garbage carbon, by the output of the discharging ship lock in the pyrolysis drum 7.
Though the utility model illustrates and describes by the reference preferred embodiment; but; those skilled in the art should understand; can be not limited to the description of present embodiment; in the scope of claims; can do the various variation on form and the details, every foundation technical spirit of the present utility model all should be thought to belong to protection domain of the present utility model to any simple modification, equivalent variations and modification that above embodiment did.
Claims (5)
1. refuse pyrolysis aerogenesis disposal plant, by refuse disposal installation, the drying garbage device, refuse pyrolysis plant, heat recovery device and smoke eliminator connect successively, it is characterized in that refuse disposal installation comprises rubbish feed bin (1), batcher (2), garbage conveyor (3), sieving garbage equipment (4) and refuse grinder (5), the drying garbage device comprises rubbish drying machine (6), refuse pyrolysis plant comprises pyrolysis drum (7), cyclone dust collectors (8), pyrolysis air burner (9) and indirect cooler (10), the heat recovery device comprises waste heat boiler (11) and steam-electric power unit (12), smoke eliminator comprises sack cleaner (13), rubbish in the rubbish feed bin (1) is sent into sieving garbage equipment (4) by batcher (2) and garbage conveyor (3), sieving garbage equipment (4) connects rubbish drying machine (6) and refuse grinder (5), rubbish drying machine (6) and refuse grinder (5) connect refuse pyrolysis drum (7), refuse pyrolysis drum (7) is provided with the charging ship lock, the pyrolysis chamber, the discharging ship lock, the pyrolysis of discharging in order to inlet plenum that the thermal decomposition thermal source is provided and discharge chamber and solid residue bloats the slag device, refuse pyrolysis drum (7) outlet connects cyclone dust collectors (8), cyclone dust collectors (8) outlet connects pyrolysis air burner (9), the outlet of pyrolysis air burner (9) is communicated with the inlet plenum and the waste heat boiler (11) of refuse pyrolysis drum (7), waste heat boiler (11) connects steam-electric power unit (12), the tail gas outlet of waste heat boiler (11) connects sack cleaner (13), and sack cleaner (13) connects chimney (14).
2. refuse pyrolysis aerogenesis disposal plant according to claim 1, it is characterized in that rubbish drying machine (6) is for having the indirect swinging drying drum of twice tube bank, heat transferring medium in the pipeline is the saturated vapor that waste heat boiler (11) produces, and there is certain angle of inclination in the rotating cylinder of rubbish drying machine.
3. refuse pyrolysis aerogenesis disposal plant according to claim 1, it is characterized in that pyrolysis drum (7) comprises a rotary barrel, cylindrical shell is outer to be rolled into a hollow chamber by refractory material, conducts heat in the chamber that the high-temperature flue gas that comes out from combustion chamber (9) forms between refractory material and rotary barrel as heating carrier.
4. refuse pyrolysis aerogenesis disposal plant according to claim 1 is characterized in that pyrolysis bloats the slag device and connects indirect cooler (10).
5. refuse pyrolysis aerogenesis disposal plant according to claim 1, it is characterized in that between drying garbage device and the refuse pyrolysis plant, pyrolysis bloats the slag device and cooling device (10) between Solid Conveying and Melting be screw feeder or conveyer belt feed.
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| CN201020533308XU CN201795494U (en) | 2010-09-17 | 2010-09-17 | Refuse pyrolysis produced gas treatment device |
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Cited By (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102658283A (en) * | 2012-05-07 | 2012-09-12 | 浙江利保环境工程有限公司 | New process for treating solid waste by taking thermal conditioning as secondary and pyrolysis as primary |
| CN102776006A (en) * | 2012-08-17 | 2012-11-14 | 江西鹏源环保科技发展有限公司 | Device for destructive distillation and drying of biomass |
| CN102896134A (en) * | 2012-08-08 | 2013-01-30 | 东南大学 | Method for producing active carbon by city household garbage and integrally using heat energy |
| CN102901102A (en) * | 2012-08-08 | 2013-01-30 | 东南大学 | Comprehensive utilization method of bio-oil prepared by city household garbage and heat energy |
| CN103712217A (en) * | 2013-12-31 | 2014-04-09 | 天津市润彤磬科技发展有限公司 | Urban garbage purifying utilizing system and garbage processing method |
| CN103759266A (en) * | 2014-01-17 | 2014-04-30 | 陈辉华 | Household garbage pyrolysis treatment method |
| CN104769680A (en) * | 2012-10-31 | 2015-07-08 | 芬兰国家技术研究中心股份公司 | Method and apparatus for treating waste material and a product gas |
| CN104879755A (en) * | 2015-04-23 | 2015-09-02 | 四川和鼎环保工程有限责任公司 | Waste incineration system |
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| CN105737163A (en) * | 2014-12-09 | 2016-07-06 | 中国科学院上海高等研究院 | Household garbage internal circulation sealed low-temperature pyrolysis system and method based on decoupling combustion |
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- 2010-09-17 CN CN201020533308XU patent/CN201795494U/en not_active Expired - Fee Related
Cited By (30)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102658283A (en) * | 2012-05-07 | 2012-09-12 | 浙江利保环境工程有限公司 | New process for treating solid waste by taking thermal conditioning as secondary and pyrolysis as primary |
| CN102658283B (en) * | 2012-05-07 | 2014-06-04 | 浙江利保环境工程有限公司 | New process for treating solid waste by taking thermal conditioning as secondary and pyrolysis as primary |
| CN102896134B (en) * | 2012-08-08 | 2014-09-10 | 东南大学 | Method for producing active carbon by city household garbage and integrally using heat energy |
| CN102896134A (en) * | 2012-08-08 | 2013-01-30 | 东南大学 | Method for producing active carbon by city household garbage and integrally using heat energy |
| CN102901102A (en) * | 2012-08-08 | 2013-01-30 | 东南大学 | Comprehensive utilization method of bio-oil prepared by city household garbage and heat energy |
| CN102776006A (en) * | 2012-08-17 | 2012-11-14 | 江西鹏源环保科技发展有限公司 | Device for destructive distillation and drying of biomass |
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| CN103712217B (en) * | 2013-12-31 | 2017-01-18 | 天津市润彤磬科技发展有限公司 | Urban garbage purifying utilizing system and garbage processing method |
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| CN105737163B (en) * | 2014-12-09 | 2020-01-07 | 中国科学院上海高等研究院 | Household garbage low-temperature pyrolysis system and method based on decoupling combustion |
| CN105737162B (en) * | 2014-12-09 | 2019-06-25 | 中国科学院上海高等研究院 | The house refuse low temperature pyrogenation system and method for Kernel-based methods decoupling and gas washing burning |
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| CN105114956B (en) * | 2015-09-16 | 2017-07-11 | 潍坊金丝达新能源科技有限公司 | High temperature garbage gasification power generation system |
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| CN105331380A (en) * | 2015-11-13 | 2016-02-17 | 北京神雾环境能源科技集团股份有限公司 | Power generation system and power generation method |
| CN105327930A (en) * | 2015-11-13 | 2016-02-17 | 北京神雾环境能源科技集团股份有限公司 | Power generation system using household garbage and power generation method thereof |
| CN105331379A (en) * | 2015-11-13 | 2016-02-17 | 北京神雾环境能源科技集团股份有限公司 | Power generation system and power generation method |
| CN107781824A (en) * | 2017-11-17 | 2018-03-09 | 华南理工大学 | A kind of high-efficiency low-pollution rural garbage method of disposal and its device |
| CN109351754A (en) * | 2018-10-29 | 2019-02-19 | 广东天源环境科技有限公司 | A kind of method and solid waste treatment system of solid waste processing |
| CN109779711A (en) * | 2019-03-29 | 2019-05-21 | 上海宝达环境科技有限公司 | A kind of garbage cracking gasification burning steam expansion power generator |
| CN111981487A (en) * | 2019-05-24 | 2020-11-24 | 梁福周 | Combustion apparatus for waste treatment and heat regeneration |
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