CN103203169A - Continuous and zero-emission organic waste processing and recycling system - Google Patents
Continuous and zero-emission organic waste processing and recycling system Download PDFInfo
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- CN103203169A CN103203169A CN2013101053143A CN201310105314A CN103203169A CN 103203169 A CN103203169 A CN 103203169A CN 2013101053143 A CN2013101053143 A CN 2013101053143A CN 201310105314 A CN201310105314 A CN 201310105314A CN 103203169 A CN103203169 A CN 103203169A
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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, relate in particular to a kind of continous way and zero-emission organic waste materials and handle the recycling system.
Background technology
Usually the compound of carbon elements is called organic compound, is called for short organic matter, except containing carbon, also contain H, O, S, N, P etc. usually during it is formed.
In recent years, the waste material of organic waste materials such as damaged tire, food-processing industry etc., these waste disposal, if directly burning produces a large amount of pernicious gases, environmental pollution causes significant impact, and adopt recycling to process, on the articulating of equipment and equipment, the energy of generation is as heat energy, all be directly to be disposed to air, waste.In addition, handle at the last pernicious gas that decomposes organic waste materials, the bigger equipment of use cost solves mostly, has both wasted electric energy in this process, and the discharge of harmful gases effect is also desirable not to the utmost.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of zero-emission, free of contamination continous way and zero-emission organic waste materials to handle the recycling system.
For solving the problems of the technologies described above, the present invention realizes by following scheme: a kind of continous way and zero-emission organic waste materials are handled the recycling system, described system can reach with the electric energy supply or combustion fire supply heat energy entirely, and reclaim heat energy and change electric energy, comprise that mainly dried apparatus for thermal cleavage, the oily vapour of advancing of feed arrangement, continous way spiral shell of connection is successively collected filter plant, tubulation cooling device, the rerun plant of band filtration, some branch temperature section cooling device, oil storage tank; The gas that organic waste materials produces after by pyrolytic is lowered the temperature by different level through some equipment, different boiling by gas liquefies, liquid separate collection after the liquefaction, another output object charcoal is directly sent into the carbon black treatment facility by the last port of export, and the heat that produces is converted into electric energy and is supplied to plant equipment again, the normal temperature fixed gas is by the liquefaction of heat energy and electric energy cooling device, and whole process is used electric energy, self heat energy, thereby reaches the zero-emission effect; Also the 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 the CO of cleaning
2Gas, and CO
2Gas converts general air to through the algae absorption and is disposed in the air, and the solid that organic waste materials produces can be delivered to carbonization manufacture recycling again, thereby reaches the zero-emission effect;
Organic waste materials is through screening or processing, pass through feed arrangement, send into the dried apparatus for thermal cleavage that advances of continous way spiral shell and carry out cracking, described continous way spiral shell is done and is advanced the 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 spiral shell do to advance apparatus for thermal cleavage inner tail end center to be provided with the 3rd device that makes a fire, be provided with first device that makes a fire in the 3rd device lower end of making a fire, described continous way spiral shell is done and is advanced the horizontal afterbody port of export of apparatus for thermal cleavage to connect the carbon black treatment facility, its vertical afterbody port of export connects oily vapour and collects filter plant, organic waste materials goes out carbon black and oily vapour through first of the charged heat energy device heating pyrolyze that makes a fire, carbon black is done by the continous way spiral shell and is advanced the apparatus for thermal cleavage tail port of export to discharge, directly send into the 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 is collected filter plant, tubulation cooling device, the rerun plant of band filtration, some branch temperature section cooling device from another port of export by oily vapour, enters oil storage tank at last;
Do the rerun plant skin that advances apparatus for thermal cleavage, oily vapour to collect filter plant, band filtration at described continous way spiral shell and be respectively equipped with heat-insulation layer; Be connected with heat-exchange device on described some each equipment of branch temperature section cooling device, described heat-exchange device is delivered to the first heat energy power-generating unit generating that is attached thereto with heat energy by high-pressure pump, a copy of it heat energy can be delivered to the freezing unit of the heat energy that is attached thereto, the low temperature that produces is in order to freezing normal temperature on-condensible gas, and this on-condensible gas is the oil gas through minute temperature section cooling device liquefies not yet;
Described continous way spiral shell is done and is advanced apparatus for thermal cleavage also to be connected with fuel gas tube, this fuel gas tube of this fuel gas tube stretches out two ports and connects second device that makes a fire respectively, the 3rd device that makes a fire, and connect some water seals by catch tank not, the described water seal other end connects and divides a temperature section cooling device;
Described continous way spiral shell is done and is advanced apparatus for thermal cleavage top also to be 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 Pai Chuing just becomes general air at last;
Described tubulation cooling device bottom is provided with this second heat-exchange device of second heat-exchange device and is connected with second thermal power generator;
The rerun plant heat-insulation layer top that described band filters is connected to the 3rd thermal power generator by exhaust pipe, and described second tail gas that makes a fire the device generation has heat energy, for the generating of the 3rd thermal power generator;
The power delivery that described the 3rd thermal power generator, second thermal power generator, the first heat energy power-generating unit produce is to motor, and the continous way spiral shell that described motor drives is attached thereto is done the apparatus for thermal cleavage work that advances.
Further, described feed arrangement top is provided with propeller, and inwall is provided with osculum and guide rail.
Further, do to advance the outer machine barrel of apparatus for thermal cleavage be single diameter or different diameter to described continous way spiral shell or misfit screw rod and directly go out machine barrel.
Further, described machine barrel is misfitted unit for turnover is arranged with diameter or different diameter or spiro rod machine tube, this unit is divided into first machine barrel and second machine barrel, in described first machine barrel and second machine barrel screw rod is installed all, the charging aperture that the product port of export of described first machine barrel connects second machine barrel is connected.
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 the width grading structure.
Further, described heating arrangements passes through with the electric power heating, or by gaseous state, liquid state, solid fuel heating.
Further, described machine barrel cooperates the screw rod design, can form a plurality of barriers, gas communication in the shielding machine barrel after being added into material.
Further, described oil storage tank is divided into low temperature oil tank, middle temperature oil tank, high temperature oil tank, and every kind of oil tank is to liquefy by the different boiling of minute temperature section cooling device by gas, is stored to low temperature oil tank, middle temperature oil tank, high temperature oil tank respectively.
Further, described tubulation cooling device, some branch temperature section cooling device are provided with the heat-insulation layer parcel separately, reach separately or join to be connected with heat-exchange device and or heat generating device together.
Advantage of the present invention is: by the heat reusing of energy source of heat exchanger generation; generate electricity; avoid energy waste; the treating apparatus of a stepping end of line gas in the end; tail gas can directly be disposed in the air, reach pollution-free purpose, convert the gas useful to air to after absorbing by the algae pond at last; both protect environment, realized energy recovery again.And the solid that organic waste materials produces can be delivered to carbonization manufacture recycling, thereby reaches the zero-emission effect.
Description of drawings
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 materials processing recycling system schematic;
Fig. 2 is feed arrangement structural representation of the present invention.
The specific embodiment
As shown in Figure 1 and Figure 2, a kind of continous way and zero-emission organic waste materials are handled the recycling system, described system can reach with the electric energy supply or combustion fire supply heat energy entirely, and reclaim heat energy and change electric energy, comprise that mainly dried apparatus for thermal cleavage 2, the oily vapour of advancing of feed arrangement 1, continous way spiral shell of connection is successively collected filter plant 3, tubulation cooling device 4, the rerun plant 7 of band filtration, the warm section of some branches cooling device 28, oil storage tank; The gas that organic waste materials produces after by pyrolytic is lowered the temperature by different level through some equipment, different boiling by gas liquefies, liquid separate collection after the liquefaction, another output object charcoal is directly sent into carbon black treatment facility 25 by the last port of export, and the heat that produces is converted into electric energy and is supplied to plant equipment again, the normal temperature fixed gas is by the liquefaction of heat energy and electric energy cooling device, and whole process is used electric energy, self heat energy, thereby reaches the zero-emission effect; Also the 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 tail gas installs the CO of 12 one-tenth cleanings after filtration
2Gas, and CO
2Gas converts general air to through the algae absorption and is disposed in the air, and the solid that organic waste materials produces can be delivered to carbonization manufacture recycling again, thereby reaches the zero-emission effect.
Organic waste materials is through screening or processing, by feed arrangement 1, send into the dried apparatus for thermal cleavage 2 that advances of continous way spiral shell and carry out cracking, described continous way spiral shell is done and is advanced apparatus for thermal cleavage 2 front ends to be provided with some exhaust outlets 13, this exhaust outlet 13 connects the 3rd thermal power generator 16, described continous way spiral shell do to advance apparatus for thermal cleavage 2 inner tail end centers to be provided with the 3rd device 31 that makes a fire, be provided with first of the charged heat energy device 26 that makes a fire in the 3rd device 31 lower ends of making a fire, described continous way spiral shell is done and is advanced the apparatus for thermal cleavage 2 horizontal afterbody ports of export to connect carbon black treatment facility 25, its vertical afterbody port of export connects oily vapour and collects filter plant 3, organic waste materials goes out carbon black and oily vapour through first of charged heat energy device 26 heating pyrolyzes that make a fire, carbon black is done by the continous way spiral shell and is advanced the apparatus for thermal cleavage 2 tail ports of export to discharge, directly send into 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 is collected filter plant 3, tubulation cooling device 4, the rerun plant 7 of band filtration, some branches temperature section cooling device 28 from another port of export by oily vapour, enters oil storage tank at last; Do rerun plant 7 skins that advance apparatus for thermal cleavage 2, oily vapour to collect filter plant 3, band filtration at described continous way spiral shell and be respectively equipped with heat-insulation layer; Be connected with heat-exchange device 29 on described some branch temperature section cooling device 28 each equipment, described heat-exchange device 29 is delivered to the first heat energy power-generating unit, 14 generatings that are attached thereto with heat energy by high-pressure pump, a copy of it heat energy can be delivered to the freezing unit 30 of the heat energy that is attached thereto, the low temperature that produces is in order to freezing normal temperature on-condensible gas, and this on-condensible gas is the oil gas through minute temperature section cooling device 28 liquefies not yet; Described continous way spiral shell is done and is advanced apparatus for thermal cleavage 2 also to be connected with fuel gas tube 20, this fuel gas tube 20 stretches out two ports and connects second device 27 that makes a fire respectively, the 3rd device 31 that makes a fire, and connect some water seals 9 by catch tank 15 not, described water seal 9 other ends connect and divide temperature section cooling device 28; Described continous way spiral shell is done and is advanced apparatus for thermal cleavage 2 tops also to be 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 Pai Chuing just becomes general air at last; Described tubulation cooling device 4 bottoms are provided with second heat-exchange device, 5 these second heat-exchange devices 5 and are connected with second thermal power generator 6; The rerun plant 7 heat-insulation layer tops that described band filters are connected to the 3rd thermal power generator 16 by exhaust pipe, and described second tail gas that makes a fire device 27 generations has heat energy, for 16 generatings of the 3rd thermal power generator; The power delivery that described second thermal power generator 16, second thermal power generator 6, the first heat energy power-generating unit 14 produce is to motor 8, and described motor 8 drives the continous way spiral shell and does apparatus for thermal cleavage 2 work that advance.Described feed arrangement 1 top is provided with propeller 101, and inwall is provided with osculum 102 and guide rail.Described continous way spiral shell do to advance apparatus for thermal cleavage 2 outer machine barrels to be single diameter or different diameter or to misfit screw rod and directly go out machine barrel.Described machine barrel is misfitted unit for turnover is arranged with diameter or different diameter or spiro rod machine tube, this unit is divided into first machine barrel and second machine barrel, in described first machine barrel and second machine barrel screw rod is installed all, the charging aperture that the product port of export of described first machine barrel connects second machine barrel is connected.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 the width grading structure.Described heating arrangements passes through with the electric power heating, or by gaseous state, liquid state, solid fuel heating.Described machine barrel cooperates the screw rod design, can form a plurality of barriers, gas communication in the shielding machine barrel after being added into material.Described oil storage tank is divided into low temperature oil tank 17, middle temperature oil tank 18, high temperature oil tank 19, and every kind of oil tank is to liquefy by the different boiling of minute temperature section cooling device 28 by gas, 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 branches temperature section cooling device 28 are provided with the heat-insulation layer parcel separately, reach separately or join with being connected with heat-exchange device to reach or heat generating device.
Energy conversion of the present invention is effectively utilized, and can reach the purpose of zero-emission, and can not cause any pollution to environment.
The above only is preferred embodiment of the present invention; be not so limit claim of the present invention; every equivalent structure or equivalent flow process conversion that utilizes specification of the present invention and accompanying drawing content to do; or directly or indirectly be used in other relevant technical field, all in like manner be included in the scope of patent protection of the present invention.
Claims (10)
1. a continous way and zero-emission organic waste materials are handled the recycling system, it is characterized in that: described system can reach with the electric energy supply or combustion fire supply heat energy entirely, and reclaim heat energy and change electric energy, comprise that mainly dried apparatus for thermal cleavage (2), the oily vapour of advancing of feed arrangement (1), continous way spiral shell of connection is successively collected filter plant (3), tubulation cooling device (4), the rerun plant (7) of band filtration, the warm section of some branches cooling device (28), oil storage tank; The gas that organic waste materials produces after by pyrolytic is lowered the temperature by different level through some equipment, different boiling by gas liquefies, liquid separate collection after the liquefaction, another output object charcoal is directly sent into carbon black treatment facility (25) by the last port of export, and the heat that produces is converted into electric energy and is supplied to plant equipment again, the normal temperature fixed gas is by the liquefaction of heat energy or electric energy cooling device, and whole process is used electric energy, self heat energy, thereby reaches the zero-emission effect; Also the 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 installs the CO that (12) become cleaning after filtration
2Gas, and CO
2Gas converts general air to through the algae absorption and is disposed in the air, and the solid that organic waste materials produces can be delivered to carbonization manufacture recycling again, thereby reaches the zero-emission effect;
Organic waste materials is through screening or processing, by feed arrangement (1), send into the dried apparatus for thermal cleavage (2) that advances of continous way spiral shell and carry out cracking, described continous way spiral shell is done and is advanced 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 spiral shell do to advance apparatus for thermal cleavage (2) inner tail end center to be provided with the 3rd device (31) that makes a fire, be provided with first device (26) that makes a fire in the 3rd device (31) lower end of making a fire, described continous way spiral shell is done and is advanced laterally afterbody port of export connection carbon black treatment facility (25) of apparatus for thermal cleavage (2), its vertical afterbody port of export connects oily vapour and collects filter plant (3), organic waste materials goes out carbon black and oily vapour through first of charged heat energy device (26) heating pyrolyze that makes a fire, carbon black is done by the continous way spiral shell and is advanced apparatus for thermal cleavage (2) the tail port of export to discharge, directly send into 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 is collected filter plant (3), tubulation cooling device (4), the rerun plant (7) of band filtration, some branches temperature section cooling device (28) from another port of export by oily vapour, enters oil storage tank at last;
Do rerun plant (7) skin that advances apparatus for thermal cleavage (2), oily vapour to collect filter plant (3), band filtration at described continous way spiral shell and be respectively equipped with heat-insulation layer; Be connected with heat-exchange device (29) on described some each equipment of branch temperature section cooling device (28), described heat-exchange device (29) is delivered to the first heat energy power-generating unit (14) generating that is attached thereto with heat energy by high-pressure pump, a copy of it heat energy can be delivered to the freezing unit of the heat energy that is attached thereto (30), the low temperature that produces is in order to freezing normal temperature on-condensible gas, and this on-condensible gas is through minute temperature section oil gas that cooling device (28) liquefies not yet;
Described continous way spiral shell is done and is advanced apparatus for thermal cleavage (2) also to be connected with fuel gas tube (20), this fuel gas tube (20) stretches out two ports and connects second device (27) that makes a fire respectively, the 3rd device (31) that makes a fire, and connecting some water seals (9) by catch tank (15) not, described water seal (9) other end connects and divides a temperature section cooling device (28);
Described continous way spiral shell is done and is advanced apparatus for thermal cleavage (2) top also to be 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 Pai Chuing just becomes general air at last;
Described tubulation cooling device (4) bottom is provided with second heat-exchange device (5), and this second heat-exchange device (5) is connected with 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, and described second tail gas that makes a fire device (27) generation has heat energy, for the 3rd thermal power generator (16) generating;
The power delivery that described the 3rd thermal power generator (16), second thermal power generator (6), the first heat energy power-generating unit (14) produce is to motor (8), and described motor (8) drives the continous way spiral shell that is attached thereto and does apparatus for thermal cleavage (2) work that advances.
2. handle the recycling system according to the described a kind of continous way of claim 1 and zero-emission organic waste materials, it is characterized in that: described feed arrangement (1) top is provided with propeller (101), and inwall is provided with osculum (102) and guide rail.
3. handle the recycling system according to the described a kind of continous way of claim 1 and zero-emission organic waste materials, it is characterized in that: described continous way spiral shell is done and advanced the outer machine barrel of apparatus for thermal cleavage (2) to be single diameter or different diameter or to misfit screw rod and directly go out machine barrel.
4. handle the recycling system according to the described a kind of continous way of claim 3 and zero-emission organic waste materials, it is characterized in that: described machine barrel is misfitted unit for turnover is arranged with diameter or different diameter or spiro rod machine tube, this unit is divided into first machine barrel and second machine barrel, in described first machine barrel and second machine barrel screw rod is installed all, the charging aperture that the product port of export of described first machine barrel connects second machine barrel is connected.
5. handle the recycling system according to the described a kind of continous way of claim 4 and zero-emission organic waste materials, it is characterized in that: described screw rod is cored screw or solid screw, and this cored screw can add heating arrangements.
6. handle the recycling system according to the described a kind of continous way of claim 4 and zero-emission organic waste materials, it is characterized in that: described screw rod is the same depth or depth gradual change or pitch is wide or the width grading structure.
7. handle the recycling system according to the described a kind of continous way of claim 5 and zero-emission organic waste materials, it is characterized in that: described heating arrangements passes through with the electric power heating, or by gaseous state, liquid state, solid fuel heating.
8. handle the recycling system according to the described a kind of continous way of claim 3 and zero-emission organic waste materials, it is characterized in that: described machine barrel cooperates the screw rod design, can form a plurality of barriers, gas communication in the shielding machine barrel after being added into material.
9. handle the recycling system according to the described a kind of continous way of claim 3 and zero-emission organic waste materials, 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), every kind of oil tank is to liquefy by the different boiling of minute temperature section cooling device (28) by gas, is stored to low temperature oil tank (17), middle temperature oil tank (18), high temperature oil tank (19) respectively.
10. handle the recycling system according to the described a kind of continous way of claim 1 and zero-emission organic waste materials, it is characterized in that: described tubulation cooling device (4), some branches temperature section cooling device (28) are provided with the heat-insulation layer parcel separately, reach separately or join with being connected with heat-exchange device to reach or heat generating device.
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| CN201310105314.3A CN103203169B (en) | 2013-03-28 | 2013-03-28 | Continuous and zero-emission organic waste processing and recycling system |
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| 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 |
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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 |
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| 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 |
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