CN103203169B - Continuous and zero-emission organic waste processing and recycling system - Google Patents
Continuous and zero-emission organic waste processing and recycling system Download PDFInfo
- Publication number
- CN103203169B CN103203169B CN201310105314.3A CN201310105314A CN103203169B CN 103203169 B CN103203169 B CN 103203169B CN 201310105314 A CN201310105314 A CN 201310105314A CN 103203169 B CN103203169 B CN 103203169B
- Authority
- CN
- China
- Prior art keywords
- continous way
- gas
- screw rod
- organic waste
- zero
- 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.)
- Expired - Fee Related
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The present invention discloses a continuous and zero-emission organic waste processing and recycling system. The system can fully use electric energy or fire to supply heat energy, recover and convert the heat energy into the electric energy. The system mainly comprises the components: a feeding device, a continuous type screw propelling thermal cracking device, an oil vapor collection and filter device, a tube cooling device, filtering and re-distilling device, a plurality of different temperature sectional cooling devices, and an oil storage jar which are connected in turn. Organic wastes are subjected to high-temperature decomposition, the generated gases are hierarchically cooled by the above devices, and then liquefied according to different boiling points of the gases, the liquefied solutions are respectively collected, and the generated heat energy is converted into the electric energy to be supplied to the mechanical equipment again, and finally the possible combustion tail gas is filtered and converted into pollution-free CO2 gas, and the CO2 gas is absorbed by algae, converted into general air and emitted outside, and moreover the solid materials generated by the organic wastes can be directly produced into carbon products for reuse, so as to achieve the zero-emission effect.
Description
Technical field
The present invention relates to a kind of energy redevelopment field, particularly relate to a kind of continous way and zero-emission organic waste process reutilization system.
Background technology
Usually the compound of carbon elements is called organic compound, is called for short organic matter, except containing except carbon in its composition, also usually containing H, O, S, N, P etc.
In recent years, organic waste materials is as the waste material etc. of damaged tire, food-processing industry, these waste disposal, if directly burning produces a large amount of pernicious gases, environmental pollution causes significant impact, and adopt recycling processing, on the articulating of equipment and equipment, the energy of generation, as heat energy, be all directly be disposed to air, waste.In addition, decomposing the last pernicious gas process of organic waste materials, the equipment that most use cost is larger solves, in this process, both wasted electric energy, and the emission effect of pernicious gas is also desirable not to the utmost.
Summary of the invention
The technical problem to be solved in the present invention there are provided a kind of zero-emission, free of contamination continous way and zero-emission organic waste process reutilization system.
For solving the problems of the technologies described above, the present invention is realized by following scheme: a kind of continous way and zero-emission organic waste process reutilization system, described system can full electric power supply or combustion fire supply heat energy, and recovery performance of changing thermal energy into electric energy, mainly comprise connect successively feed arrangement, continous way screw rod advance apparatus for thermal cleavage, oily vapour collect filter plant, tubulation cooling device, band filter rerun plant, some points of warm section cooling devices, oil storage tanks; Organic waste materials is lowered the temperature through some equipment by different level by the gas produced after pyrolytic, liquefy by the different boiling of gas, the liquid separate collection of post liquefaction, another output object charcoal directly sends into carbon black treatment facility by the last port of export, and the converting heat produced is that electric energy is supplied to plant equipment again, normal temperature fixed gas is liquefied by heat energy and electric energy cooling device, and whole process uses electric energy, self heat energy, thus reaches zero-emission effect; Also normal temperature fixed gas can be delivered to first device, second device, the 3rd that makes a fire that makes a fire and make a fire device as heat energy, and tail gas after filtration device become clean CO
2gas, and CO
2gas absorbs through algae and converts general air venting to in air, and the solid that organic waste materials produces can deliver to again carbonization manufacture recycling, thus reaches zero-emission effect;
Organic waste materials is through screening or process, pass through feed arrangement, sending into continous way screw rod advances apparatus for thermal cleavage to carry out cracking, described continous way screw rod advances apparatus for thermal cleavage front end to be provided with some exhaust outlets, this exhaust outlet connects the 3rd thermal power generator, described continous way screw rod advances apparatus for thermal cleavage inner tail end center to be provided with the 3rd and to make a fire device, be provided with first make a fire device in the 3rd device lower end of making a fire, described continous way screw rod advances the horizontal afterbody port of export of apparatus for thermal cleavage to connect carbon black treatment facility, its vertical afterbody port of export connects oily vapour and collects filter plant, first of the organic waste materials band electrical heat energy device heating pyrolyze that makes a fire goes out carbon black and oily vapour, carbon black advances the apparatus for thermal cleavage tail port of export to discharge by continous way screw rod, direct feeding carbon black treatment facility, carbon black can be processed into the charcoal finished product of multiple different purposes according to the difference of its quality, oil vapour collects rerun plant, the some points of warm section cooling devices of filter plant, tubulation cooling device, band filtration by oily vapour from another port of export, finally enter oil storage tank,
The rerun plant skin that apparatus for thermal cleavage, oily vapour collect filter plant, band filters is advanced to be respectively equipped with heat-insulation layer at described continous way screw rod; The described some points of each equipment of warm section cooling device are connected with heat-exchange device, heat energy is delivered to the first heat energy power-generating unit generating be attached thereto by described heat-exchange device by high-pressure pump, a copy of it heat energy can deliver to the freezing unit of the heat energy be attached thereto, the low temperature produced is in order to freezing normal temperature on-condensible gas, and this on-condensible gas is the oil gas liquefied not yet through point warm section cooling device;
Described continous way screw rod advances apparatus for thermal cleavage to be also connected with fuel gas tube, this fuel gas tube of this fuel gas tube stretches out two ports and connects second device, the 3rd that makes a fire respectively and to make a fire device, and connecting some water seals by not catch tank, the described water seal other end connects a point warm section cooling device;
Described continous way screw rod advances apparatus for thermal cleavage top to be also provided with offgas duct, and this offgas duct end connects the 3rd thermal power generator, tail gas filter and green alga pond successively, and the gas of finally discharging just becomes general air;
Described tubulation cooling device bottom is provided with this second heat-exchange device of the second heat-exchange device and is connected with the second thermal power generator;
Described band filter rerun plant heat-insulation layer top be connected to the 3rd thermal power generator by exhaust pipe, described second make a fire device produce tail gas with heat energy, for the 3rd thermal power generator generating;
The electric energy that described 3rd thermal power generator, the second thermal power generator, the first heat energy power-generating unit produce is delivered to motor, and described motor drives the continous way screw rod be attached thereto to advance apparatus for thermal cleavage work.
Further, described feed arrangement top is provided with screw, and inwall is provided with osculum and guide rail.
Further, described continous way screw rod advances the outer machine barrel of apparatus for thermal cleavage to be single diameter or different diameter or misfits screw rod and directly go out machine barrel.
Further, described machine barrel misfits unit for there being turnover with diameter or different diameter or spiro rod machine tube, this unit is divided into the first machine barrel and the second machine barrel, is all provided with screw rod in described first machine barrel and the second machine barrel, and the product port of export of described first machine barrel connects the charging aperture of the second machine barrel.
Further, described screw rod is cored screw or solid screw, and this cored screw can add heating arrangements.
Further, described screw rod is the same depth or depth gradual change or pitch is wide or width grading structure.
Further, described heating arrangements by heating with electric power, or is heated by gaseous state, liquid state, solid fuel.
Further, described machine barrel coordinates screw design, can form multiple barrier after being added into material, gas circulation in shielding machine barrel.
Further, described oil storage tank is divided into low temperature oil tank, middle temperature oil tank, high temperature oil tank, often kind of oil tank is liquefied by the different boiling of gas by a point warm section cooling device, and the liquid generated after gas liquefaction, is stored to low temperature oil tank, middle temperature oil tank, high temperature oil tank respectively.
Further, described tubulation cooling device, some points of warm section cooling devices are provided with heat-insulation layer parcel separately, and separately or connection with being connected with heat-exchange device or heat generating device.
Advantage of the present invention is: the heat reusing of energy source produced by heat exchanger; generate electricity; avoid energy waste; the in the end treating apparatus of a stepping end of line gas; make tail gas directly be disposed in air, reach pollution-free object, after absorbing finally by algae pond, convert the gas useful to air to; both protect environment, realize energy recovery again.And the solid that organic waste materials produces can deliver to carbonization manufacture recycling, thus reach zero-emission effect.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the present invention is elaborated.
Fig. 1 is continous way of the present invention and zero-emission organic waste process reutilization system schematic diagram;
Fig. 2 is feed arrangement structural representation of the present invention.
Detailed description of the invention
As shown in Figure 1 and Figure 2, a kind of continous way and zero-emission organic waste process reutilization system, described system can full electric power supply or combustion fire supply heat energy, and recovery performance of changing thermal energy into electric energy, mainly comprise connect successively feed arrangement 1, continous way screw rod advance apparatus for thermal cleavage 2, oily vapour collect filter plant 3, tubulation cooling device 4, band filter rerun plant 7, some points of warm section cooling devices 28, oil storage tanks; Organic waste materials is lowered the temperature through some equipment by different level by the gas produced after pyrolytic, liquefy by the different boiling of gas, the liquid separate collection of post liquefaction, another output object charcoal directly sends into carbon black treatment facility 25 by the last port of export, and the converting heat produced is that electric energy is supplied to plant equipment again, normal temperature fixed gas is liquefied by heat energy and electric energy cooling device, and whole process uses electric energy, self heat energy, thus reaches zero-emission effect; Also normal temperature fixed gas can be delivered to first device 26, second device 27, the 3rd that makes a fire that makes a fire and make a fire device 27 as heat energy, and the tail gas CO that 12 one-tenth, device is clean after filtration
2gas, and CO
2gas absorbs through algae and converts general air venting to in air, and the solid that organic waste materials produces can deliver to again carbonization manufacture recycling, thus reaches zero-emission effect.
Organic waste materials is through screening or process, by feed arrangement 1, sending into continous way screw rod advances apparatus for thermal cleavage 2 to carry out cracking, described continous way screw rod advances apparatus for thermal cleavage 2 front end to be provided with some exhaust outlets 13, this exhaust outlet 13 connects the 3rd thermal power generator 16, described continous way screw rod advances apparatus for thermal cleavage 2 inner tail end center to be provided with the 3rd and to make a fire device 31, be provided with first of band electrical heat energy make a fire device 26 in the 3rd device 31 lower end of making a fire, described continous way screw rod advances the horizontal afterbody port of export of apparatus for thermal cleavage 2 to connect carbon black treatment facility 25, its vertical afterbody port of export connects oily vapour and collects filter plant 3, first of organic waste materials band electrical heat energy device 26 heating pyrolyze that makes a fire goes out carbon black and oily vapour, carbon black advances the apparatus for thermal cleavage 2 tail port of export to discharge by continous way screw rod, direct feeding carbon black treatment facility 25, carbon black can be processed into the charcoal finished product of multiple different purposes according to the difference of its quality, oil vapour collects rerun plant 7, the some points of warm section cooling devices 28 of filter plant 3, tubulation cooling device 4, band filtration by oily vapour from another port of export, finally enter oil storage tank, rerun plant 7 skin that apparatus for thermal cleavage 2, oily vapour collect filter plant 3, band filters is advanced to be respectively equipped with heat-insulation layer at described continous way screw rod, the described some points of each equipment of warm section cooling device 28 are connected with heat-exchange device 29, heat energy is delivered to by high-pressure pump the first heat energy power-generating unit 14 be attached thereto and is generated electricity by described heat-exchange device 29, a copy of it heat energy can deliver to the freezing unit 30 of the heat energy be attached thereto, the low temperature produced is in order to freezing normal temperature on-condensible gas, and this on-condensible gas is the oil gas liquefied not yet through point warm section cooling device 28, described continous way screw rod advances apparatus for thermal cleavage 2 to be also connected with fuel gas tube 20, this fuel gas tube 20 stretches out two ports and connects second device 27, the 3rd that makes a fire respectively and to make a fire device 31, and connecting some water seals 9 by not catch tank 15, described water seal 9 other end connects a point warm section cooling device 28, described continous way screw rod advances apparatus for thermal cleavage 2 top to be also provided with offgas duct, and this offgas duct end connects the 3rd thermal power generator 16, tail gas filter 12 and green alga pond 10 successively, and the gas of finally discharging just becomes general air, described tubulation cooling device 4 bottom is provided with this second heat-exchange device 5 of the second heat-exchange device 5 and is connected with the second thermal power generator 6, the rerun plant 7 heat-insulation layer top that described band filters is connected to the 3rd thermal power generator 16 by exhaust pipe, and described second makes a fire tail gas that device 27 produces, with heat energy, generates electricity for the 3rd thermal power generator 16, the electric energy that described second thermal power generator 16, second thermal power generator 6, first heat energy power-generating unit 14 produces is delivered to motor 8, and described motor 8 drives continous way screw rod to advance apparatus for thermal cleavage 2 to work.Described feed arrangement 1 top is provided with screw 101, and inwall is provided with osculum 102 and guide rail.Described continous way screw rod advances the outer machine barrel of apparatus for thermal cleavage 2 to be single diameter or different diameter or misfits screw rod and directly go out machine barrel.Described machine barrel misfits unit for there being turnover with diameter or different diameter or spiro rod machine tube, this unit is divided into the first machine barrel and the second machine barrel, all be provided with screw rod in described first machine barrel and the second machine barrel, the product port of export of described first machine barrel connects the charging aperture of the second machine barrel.Described screw rod is cored screw or solid screw, and this cored screw can add heating arrangements.Described screw rod is the same depth or depth gradual change or pitch is wide or width grading structure.Described heating arrangements by heating with electric power, or is heated by gaseous state, liquid state, solid fuel.Described machine barrel coordinates screw design, can form multiple barrier after being added into material, gas circulation in shielding machine barrel.Described oil storage tank is divided into low temperature oil tank 17, middle temperature oil tank 18, high temperature oil tank 19, often kind of oil tank is liquefied by the different boiling of gas by a point warm section cooling device 28, the liquid generated after gas liquefaction, is stored to low temperature oil tank 17, middle temperature oil tank 18, high temperature oil tank 19 respectively.Described tubulation cooling device 4, some points of warm section cooling devices 28 are provided with heat-insulation layer parcel separately, and separately or connection with being connected with heat-exchange device or heat generating device.
Energy conversion of the present invention effectively utilizes, and can reach the object of zero-emission, and can not cause any pollution to environment.
The foregoing is only the preferred embodiment of the present invention; not thereby the scope of the claims of the present invention is limited; every utilize description of the present invention and accompanying drawing content to do equivalent structure or equivalent flow process conversion; or be directly or indirectly used in other relevant technical field, be all in like manner included in scope of patent protection of the present invention.
Claims (10)
1. a continous way and zero-emission organic waste process reutilization system, it is characterized in that: described system can full electric power supply or combustion fire supply heat energy, and recovery performance of changing thermal energy into electric energy, mainly comprise that the feed arrangement (1), the continous way screw rod that connect successively advance that apparatus for thermal cleavage (2), oily vapour collect filter plant (3), the rerun plant (7) that tubulation cooling device (4), band filter, some points of warm section cooling devices (28), oil storage tank; Organic waste materials is lowered the temperature through some equipment by different level by the gas produced after pyrolytic, liquefy by the different boiling of gas, the liquid separate collection of post liquefaction, another output object charcoal directly sends into carbon black treatment facility (25) by the last port of export, and the converting heat produced is that electric energy is supplied to plant equipment again, normal temperature fixed gas is liquefied by heat energy or electric energy cooling device, and whole process uses electric energy, self heat energy, thus reaches zero-emission effect; Also normal temperature fixed gas can be delivered to first device (26), second device (27), the 3rd that makes a fire that makes a fire and make a fire device (31) as heat energy, and tail gas after filtration device (12) become clean CO
2gas, and CO
2gas absorbs through algae and converts general air venting to in air, and the solid that organic waste materials produces can deliver to again carbonization manufacture recycling, thus reaches zero-emission effect;
Organic waste materials is through screening or process, by feed arrangement (1), sending into continous way screw rod advances apparatus for thermal cleavage (2) to carry out cracking, described continous way screw rod advances apparatus for thermal cleavage (2) front end to be provided with some exhaust outlets (13), this exhaust outlet (13) connects the 3rd thermal power generator (16), described continous way screw rod advances apparatus for thermal cleavage (2) inner tail end center to be provided with the 3rd and to make a fire device (31), be provided with first make a fire device (26) in the 3rd device (31) lower end of making a fire, described continous way screw rod advances the horizontal afterbody port of export of apparatus for thermal cleavage (2) to connect carbon black treatment facility (25), its vertical afterbody port of export connects oily vapour and collects filter plant (3), first of organic waste materials band electrical heat energy device (26) heating pyrolyze that makes a fire goes out carbon black and oily vapour, carbon black advances apparatus for thermal cleavage (2) the tail port of export to discharge by continous way screw rod, direct feeding carbon black treatment facility (25), carbon black can be processed into the charcoal finished product of multiple different purposes according to the difference of its quality, oil vapour collects filter plant (3), tubulation cooling device (4), the rerun plant (7) of band filtration, some points of warm section cooling devices (28) from another port of export by oily vapour, finally enters oil storage tank,
Rerun plant (7) skin that apparatus for thermal cleavage (2), oily vapour collect filter plant (3), band filters is advanced to be respectively equipped with heat-insulation layer at described continous way screw rod; The described some points of each equipment of warm section cooling device (28) are connected with heat-exchange device (29), heat energy is delivered to the first heat energy power-generating unit (14) generating be attached thereto by described heat-exchange device (29) by high-pressure pump, a copy of it heat energy can deliver to the freezing unit of the heat energy be attached thereto (30), the low temperature produced is in order to freezing normal temperature on-condensible gas, and this on-condensible gas is the oil gas liquefied not yet through point warm section cooling device (28);
Described continous way screw rod advances apparatus for thermal cleavage (2) to be also connected with fuel gas tube (20), this fuel gas tube (20) stretches out two ports and connects second device (27), the 3rd that makes a fire respectively and to make a fire device (31), and connecting some water seals (9) by not catch tank (15), described water seal (9) other end connects a point warm section cooling device (28);
Described continous way screw rod advances apparatus for thermal cleavage (2) top to be also provided with offgas duct, this offgas duct end connects the 3rd thermal power generator (16), tail gas filter (12) and green alga pond (10) successively, and the gas of finally discharging just becomes general air;
Described tubulation cooling device (4) bottom is provided with the second heat-exchange device (5), and this second heat-exchange device (5) is connected with the second thermal power generator (6);
Rerun plant (7) the heat-insulation layer top that described band filters is connected to the 3rd thermal power generator (16) by exhaust pipe, described second makes a fire tail gas that device (27) produces with heat energy, for the 3rd thermal power generator (16) generating;
The electric energy that described 3rd thermal power generator (16), the second thermal power generator (6), the first heat energy power-generating unit (14) produce is delivered to motor (8), and described motor (8) drives the continous way screw rod be attached thereto to advance apparatus for thermal cleavage (2) work.
2. according to a kind of continous way according to claim 1 and zero-emission organic waste process reutilization system, it is characterized in that: described feed arrangement (1) top is provided with screw (101), inwall is provided with osculum (102) and guide rail.
3. according to a kind of continous way according to claim 1 and zero-emission organic waste process reutilization system, it is characterized in that: described continous way screw rod advances apparatus for thermal cleavage (2) outer machine barrel to be single diameter or different diameter or misfits screw rod and directly go out machine barrel.
4. according to a kind of continous way according to claim 3 and zero-emission organic waste process reutilization system, it is characterized in that: described machine barrel misfits unit for there being turnover with diameter or different diameter or spiro rod machine tube, this unit is divided into the first machine barrel and the second machine barrel, all be provided with screw rod in described first machine barrel and the second machine barrel, the product port of export of described first machine barrel connects the charging aperture of the second machine barrel.
5. according to a kind of continous way according to claim 4 and zero-emission organic waste process reutilization system, it is characterized in that: described screw rod is cored screw or solid screw, and this cored screw can add heating arrangements.
6. according to a kind of continous way according to claim 4 and zero-emission organic waste process reutilization system, it is characterized in that: described screw rod is the same depth or depth gradual change or pitch is wide or width grading structure.
7. according to a kind of continous way according to claim 5 and zero-emission organic waste process reutilization system, it is characterized in that: described heating arrangements by heating with electric power, or is heated by gaseous state, liquid state, solid fuel.
8. according to a kind of continous way according to claim 3 and zero-emission organic waste process reutilization system, it is characterized in that: described machine barrel coordinates screw design, can form multiple barrier after being added into material, gas circulation in shielding machine barrel.
9. according to a kind of continous way according to claim 3 and zero-emission organic waste process reutilization system, it is characterized in that: described oil storage tank is divided into low temperature oil tank (17), middle temperature oil tank (18), high temperature oil tank (19), often kind of oil tank is liquefied by the different boiling of gas by a point warm section cooling device (28), the liquid generated after gas liquefaction, is stored to low temperature oil tank (17), middle temperature oil tank (18), high temperature oil tank (19) respectively.
10. according to a kind of continous way according to claim 1 and zero-emission organic waste process reutilization system, it is characterized in that: described tubulation cooling device (4), some points of warm section cooling devices (28) are provided with heat-insulation layer parcel separately, and separately or connection with being connected with heat-exchange device or heat generating device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310105314.3A CN103203169B (en) | 2013-03-28 | 2013-03-28 | Continuous and zero-emission organic waste processing and recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310105314.3A CN103203169B (en) | 2013-03-28 | 2013-03-28 | Continuous and zero-emission organic waste processing and recycling system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103203169A CN103203169A (en) | 2013-07-17 |
| CN103203169B true CN103203169B (en) | 2015-04-15 |
Family
ID=48750700
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310105314.3A Expired - Fee Related CN103203169B (en) | 2013-03-28 | 2013-03-28 | Continuous and zero-emission organic waste processing and recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103203169B (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1392224A (en) * | 2001-06-14 | 2003-01-22 | 上海市环境工程设计科学研究院 | Oil refining process of waste plastic and equipment |
| JP2005194351A (en) * | 2004-01-05 | 2005-07-21 | Nippon Steel Corp | Method for removing pyrolytic carbon from dry distillation gas of organic waste |
| CN101307288A (en) * | 2008-02-14 | 2008-11-19 | 朱洪 | Process and equipment for preparing biological energy source |
| WO2009103254A1 (en) * | 2008-02-23 | 2009-08-27 | SWU Gesellschaft für Umwelttechnik mbH | Process for the pyrolysis of organic waste substances and biomaterials |
| CN101525551A (en) * | 2008-03-05 | 2009-09-09 | 饶文涛 | Method for preparing biofuel by using flue gases as raw materials |
| CN101851523A (en) * | 2010-06-01 | 2010-10-06 | 上海劲飚环保科技有限公司 | Continuous waste plastics refining unit |
| CN102618315A (en) * | 2011-01-31 | 2012-08-01 | 林慕清 | Recovery device of waste and old plastic and rubber by cracking |
-
2013
- 2013-03-28 CN CN201310105314.3A patent/CN103203169B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1392224A (en) * | 2001-06-14 | 2003-01-22 | 上海市环境工程设计科学研究院 | Oil refining process of waste plastic and equipment |
| JP2005194351A (en) * | 2004-01-05 | 2005-07-21 | Nippon Steel Corp | Method for removing pyrolytic carbon from dry distillation gas of organic waste |
| CN101307288A (en) * | 2008-02-14 | 2008-11-19 | 朱洪 | Process and equipment for preparing biological energy source |
| WO2009103254A1 (en) * | 2008-02-23 | 2009-08-27 | SWU Gesellschaft für Umwelttechnik mbH | Process for the pyrolysis of organic waste substances and biomaterials |
| CN101525551A (en) * | 2008-03-05 | 2009-09-09 | 饶文涛 | Method for preparing biofuel by using flue gases as raw materials |
| CN101851523A (en) * | 2010-06-01 | 2010-10-06 | 上海劲飚环保科技有限公司 | Continuous waste plastics refining unit |
| CN102618315A (en) * | 2011-01-31 | 2012-08-01 | 林慕清 | Recovery device of waste and old plastic and rubber by cracking |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103203169A (en) | 2013-07-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US20150147242A1 (en) | Carbon-based durable goods and renewable fuel from biomass waste dissociation | |
| RU2616196C2 (en) | Structural scheme and environmentally safe method of processing wastes and biomass to increase efficiency of generating electric power and heat | |
| CN103409171A (en) | Biomass pressurized fluidized bed gasification gas turbine combined cycle power generation system | |
| CN102061196A (en) | Power generation method and device adopting plasma gasification of household garbage and biomass | |
| CN101531910A (en) | System for rapidly pyrolysing and liquefying biomass | |
| CN203403070U (en) | Biomass pressurized fluidized-bed gasification gas turbine combined cycle power generation system | |
| CN101017022A (en) | Novel technology for directly using charring gas of biomass as boiler fuel | |
| CN101775314B (en) | Biomass carbonizing, gasifying and generating process and movable carbonization and gasification furnaces | |
| CN108977218A (en) | A kind of greasy filth/scrap rubber innocuity disposal system and its continuous separation device | |
| CN102389887A (en) | High-temperature treatment and super-high-temperature plasma gasification method of municipal domestic wastes | |
| CN107723003B (en) | Organic matter carbonization system and method thereof | |
| CN103203169B (en) | Continuous and zero-emission organic waste processing and recycling system | |
| CN203220846U (en) | Continuous type zero-discharge organic waste material treatment recycling system | |
| CN201198470Y (en) | Biomass rapid pyrolysis liquefaction system | |
| CN105694926A (en) | Destructive distillation conversion treatment system for household refuse | |
| KR20180016024A (en) | A kind of the lower absorption type intermittent consecutive injection of immobilized gasification machine for disposal plastic and organic household waste | |
| CN100563857C (en) | The method of separating hydrargyrum and cracking organic substances | |
| CN205603520U (en) | Domestic waste dry distillation conversion processing system | |
| CN101974351A (en) | Scale fixed bed biomass gasification power generation production technology and complete equipment | |
| CN202688284U (en) | Fluidized bed biomass gasification electrical power generating system | |
| CN104548870B (en) | Oil gas treatment system | |
| CN204381054U (en) | A kind of device processing organic waste | |
| CN107274952B (en) | Treatment system of medium-low radioactivity nuclear waste and power generation system with same | |
| CN107755402B (en) | Catalytic hydrogen production device from municipal solid waste | |
| CN204779495U (en) | Use device of rubbish charcoal as raw materials preparation gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150415 Termination date: 20180328 |