CN207756595U - A kind of electricity generation system of debirs clean utilization - Google Patents
A kind of electricity generation system of debirs clean utilization Download PDFInfo
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- CN207756595U CN207756595U CN201721593886.0U CN201721593886U CN207756595U CN 207756595 U CN207756595 U CN 207756595U CN 201721593886 U CN201721593886 U CN 201721593886U CN 207756595 U CN207756595 U CN 207756595U
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- 230000005611 electricity Effects 0.000 title claims abstract description 38
- 238000005336 cracking Methods 0.000 claims abstract description 53
- 238000000197 pyrolysis Methods 0.000 claims abstract description 38
- 239000007789 gas Substances 0.000 claims description 78
- 239000002918 waste heat Substances 0.000 claims description 12
- 238000006243 chemical reaction Methods 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract description 8
- 238000000034 method Methods 0.000 abstract description 8
- 239000002699 waste material Substances 0.000 abstract description 7
- 238000004064 recycling Methods 0.000 abstract description 4
- 230000009466 transformation Effects 0.000 abstract description 3
- 239000010815 organic waste Substances 0.000 description 26
- 239000000203 mixture Substances 0.000 description 13
- 238000001035 drying Methods 0.000 description 12
- 239000002737 fuel gas Substances 0.000 description 9
- 239000000567 combustion gas Substances 0.000 description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 238000009833 condensation Methods 0.000 description 6
- 230000005494 condensation Effects 0.000 description 6
- 239000008234 soft water Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 241001465754 Metazoa Species 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 238000012856 packing Methods 0.000 description 3
- 239000011236 particulate material Substances 0.000 description 3
- 230000000505 pernicious effect Effects 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 240000004859 Gamochaeta purpurea Species 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 208000021267 infertility disease Diseases 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- DOTMOQHOJINYBL-UHFFFAOYSA-N molecular nitrogen;molecular oxygen Chemical compound N#N.O=O DOTMOQHOJINYBL-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002881 soil fertilizer Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model is related to environment comprehensive pollution treatment and waste recycling field more particularly to a kind of electricity generation systems and method of debirs clean utilization.A kind of electricity generation system of debirs clean utilization, including dryer, comminutor, pyrolysis furnace, semicoke cooler, cracking Gas Cooler, separator and gas electricity generator；Further include air blower, air blower is connected with heat exchanger tube, and heat exchanger tube is connect after semicoke cooler and cracking Gas Cooler with the air inlet of dryer successively.The utility model can improve the electricity generation system and method for debirs energy conversion efficiency while providing a kind of energy saving, solve the problems, such as that existing debirs electricity generation system energy consumption is high, energy transformation ratio is low.
Description
Technical field
The utility model is related to environment comprehensive pollution treatment and waste recycling field more particularly to a kind of debirs are clear
The clean electricity generation system utilized.
Background technology
Electricity has become one of the necessary energy indispensable in today's society, is a kind of good secondary energy sources, it is clear
It is clean, conveniently, utilization rate it is high.One national per capita household electricity consumption number indicate the level of economic development and the people's life of this country
Running water is flat, although China's per capita household electricity consumption has been approached world average level, only the 1/4~1/5 of Systems in Certain Developed Countries, gap
Obviously, electric market is still huge.
Although electricity is high-quality, cleaning, it needs primary energy, China still to generate electricity at present with fossil energy (firepower) after all
Based on, environmental pollution is a great problem of current thermal power generation, on the one hand pollutes air, polluted source, on the one hand expends again
Valuable coal resources.980,000 tons of China's electric power Air Pollutants Emissions flue dust, 6,200,000 tons of sulfur dioxide, nitrogen oxygen in 2014
6,200,000 tons of compound, such serious pollution threat of data our health.
In recent years, with the fast development of national economy, the industrialization of the country, urbanization realization step by step, rural area labour
Right-about also has occurred with burning in the transfer of power, the transformation of life style, fertilising, excrement of animals be no longer soil fertilizer,
Straw is no longer the fuel and feed in rural area, all becomes organic waste, can not be burned in addition, powerless returning to the field, infertile field,
It stacks and topples over everywhere in field, it is everlasting to rot to send out a burst of stink, pollute environment；According to statistics, China is every
More than 700,000,000 tons of stalk can be produced year, 1,500,000 tons of excrement of animals is lost in addition in the annual municipal refuse for producing 1.5 hundred million tons per year in China
Up to 25,000,000,000 yuan of " renewable resource " value abandoned directly burns and recycles heat generation steam by boiler, sent out by steam turbine
Electricity, can capacity usage ratio less than 25%, also generate bioxin, flying dust etc. causes secondary pollution to air.
Number of patent application is that the patent of invention of CN200310115199.4 discloses a kind of while handling a variety of debirs
Plasma multi-stage cleavage method and device.This method includes that level-one plasma pyrolysis stove uses reproducibility working gas,
The tail gas of generation is imflammable gas, and into two level pyrolysis furnace, supplementary energy is provided for two level pyrolysis furnace.Two level pyrolysis furnace uses
Oxidisability working gas can save power consumption；If using parallel arrangement, and pyrolysis furnace and two level pyrolysis furnace can be with
Using a set of tail gas treatment device.The tail gas of the level-one pyrolysis furnace of arranged in series can pass through washing and neutralize sour gas into two
Grade pyrolysis furnace is as auxiliary fuel；The imflammable gas of two level pyrolysis furnace discharge is post-treated, is sent to burner combustion or power generation
Machine generates electricity.At least one air inlet is arranged in the bottom of two level pyrolysis furnace provided by the utility model, therefore can be by increasing gas
Body supply improves cracking temperature, the advantages of reaching energy saving and time；Two-stage pyrolysis furnace can according to integrated design,
Form combined furnace body.
Above-mentioned apparatus is realized while being handled the purpose of a variety of debirs by multistage cracking, but and routine organic waste
Object cracking treating device is identical, and tar steam and vapor are contained in the cracking gas that above-mentioned apparatus generates, to the combustion of cracking gas
It is relatively low to heat value.When cracking gas generates electricity for gas electricity generator, above-mentioned cracking gas because contain tar steam and vapor without
It can be fully burned, on the one hand, increase the discharge of pernicious gas；Another reverse side, cracking gas fail to be fully used, have
The energy conversion efficiency of machine waste is relatively low.
Utility model content
The utility model overcomes the deficiencies in the prior art, and debirs energy can be improved while providing a kind of energy saving and is turned
The electricity generation system and method for changing efficiency solve the problems, such as that existing debirs electricity generation system energy consumption is high, energy transformation ratio is low.
In order to solve the above technical problems, the utility model uses following technical scheme：
A kind of electricity generation system of debirs clean utilization, including dryer, dryer are connected with by screw conveyor
Comminutor, comminutor are connected with pyrolysis furnace by belt conveyor；Pyrolysis furnace is connected with semicoke cooler by screw conveyor,
Pyrolysis furnace is connected with cracking Gas Cooler by pipeline, and the outlet for cracking cooler is connected with separator and combustion in turn by pipeline
Gas generator, generator are electrically connected with electrical appliance；Further include air blower, the air outlet of air blower is connected with heat exchanger tube, heat exchanger tube
It is connect successively with the air inlet of dryer after semicoke cooler and cracking Gas Cooler.
As the preferred embodiment of the utility model, the exhaust outlet of the generator is connected with waste heat boiler by pipeline, remaining
The steam (vapor) outlet of heat boiler and the air inlet of pyrolysis furnace are connected by pipeline.
As the preferred embodiment of the utility model, the feed inlet of the dryer is connected with by screw conveyor for filtering
The filter press of slag.
As the preferred embodiment of the utility model, the exhaust outlet of the dryer is connected with clarifier by pipeline.
Compared with prior art, the utility model has the beneficial effects that：
1, the utility model recycles the heat of pyrolysis product, is used for drying material, makes the heat generated in system
Amount is utilized effectively, and reduces energy consumption.Also, when the heat to cracking gas exchanges heat, the tar steam in cracking gas
Condensation sedimentation is obtained with vapor, is purified to cracking gas, cracking gas not containing water vapor and when tar steam, calorific value obtains
To significantly improving.After condensation separation, the calorific value of cracking gas reaches 14000kj/Nm3~16000kj/Nm3, and without cold
The calorific value of the cracking gas of solidifying separation is only 9000kj/Nm3~12000kj/Nm3.In the case where cracking gas calorific value raising, phase
Debirs energy conversion efficiency should be improved, tool has an unexpected effect.
2 the utility model are utilized organic waste as resource, are solved organic waste and are caused to environment
Pollution, while save organic waste occupancy land resource.Cracking gas when being disposed to organic waste cracking, passes through
Gas electricity generator carries out the direct generation of electricity, improves generating efficiency, avoids the secondary pollution caused by environment, prevents bioxin
With the generation of dust.
3, fuel gas buring generate high temperature carbon dioxide and vapor formed high-temperature gas mixture stream, high-temperature gas mixture stream into
Soft water heat exchange in waste heat boiler, with boiler, soft water absorption heat become steam.Steam is transported to pyrolysis furnace, lazy as packing
Property gas, ensures the safety of pyrolysis furnace.To which the heat of fuel gas buring is utilized effectively, and reduces the energy consumption of system.
4, clarifier can evolve to the tail gas being discharged in dryer, reduce the discharge of pernicious gas.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
Specific implementation mode
Below in conjunction with the accompanying drawings, the utility model is described in detail.
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation
Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only explaining this
Utility model is not used to limit the utility model.
The specific implementation process of the utility model：
First, organic waste carries out press filtration through filter press, closed defeated by screw conveyor after removing most of moisture
It send to dryer.The drying organic waste exported from dryer, is sent into comminutor and is granulated, dry organic waste is made
Gurry particulate material.
Second, organic waste particulate material and the air exclusion in pyrolysis furnace are will be delivered to, is added with Electric heating
Heat arrives certain temperature condition.Cracking reaction occurs for organic waste particulate material, is transformed into high-temperature combustible gas body and part high temperature half
It is burnt.
Air needed for drying is first fed into semicoke cooler by third, air blower, and the hot semicoke to come is conveyed with pyrolysis furnace
It exchanges heat, semicoke is cooled down.Air is heated to certain temperature, then is come with pyrolysis furnace conveying by cracking Gas Cooler
High-temperature gas carry out indirect heat exchange, the part tar steam in Pintsch process gas is condensed into tar, Water vapor condensation, combustion gas
It is cooled down.Meanwhile air further absorbs heat after heating up, and is sent into dryer, as drying medium, for organic waste
It is dried.Moisture heat absorption evaporation in organic waste becomes steam, net by purified device together with drying medium air
Change, then outer row.
4th, the purification cracking gas obtained after refrigerated separation is sent into gas electricity generator, cracking gas is in gas electricity generator cylinder
Combustion reaction is carried out with air filtering excessively in vivo, releases a large amount of heat.Combustion gas volume in the cylinder body of gas electricity generator suddenly
Expansion pushes piston externally to do work, and driving generator amature makees cutting magnetic line rotation in magnetic field and generates electric current.The electricity of generation
Streaming is to electrical appliance, by electrical appliance continuous and stable to national grid output current.
5th, fuel gas buring generates high temperature carbon dioxide and vapor forms high-temperature gas mixture stream.By high-temperature gas mixture stream
It is sent into waste heat boiler, high-temperature gas mixture stream exchanges heat with the soft water in waste heat boiler, and soft water absorption heat becomes steam.Steam conveys
Ensure the safety of pyrolysis furnace as packing inert gas to pyrolysis furnace.
Above-mentioned implementation process solves the problems, such as that organic waste pollutes the environment, while also achieving organic
The recycling of waste, turns waste into wealth, and does not have " three wastes " externally to discharge, and is a kind of clean generation mode.The utility model
The energy of renewable resource is adequately utilized, new outlet is had found to administer organic waste environmental pollution, in system
Waste heat be utilized effectively, reduce energy consumption.Most of all, in the waste heat using combustible gas mixture and semicoke to original
When material is dried, the cracking gas calorific value in fuel gas mixture is improved significantly, and correspondingly, improves the energy of debirs
Conversion ratio.
Embodiment one
As shown in Figure 1, a kind of electricity generation system of debirs clean utilization, including dryer, dryer pass through spiral transferring
Machine is sent to be connected with comminutor, comminutor is connected with pyrolysis furnace by belt conveyor；Pyrolysis furnace is connected with by screw conveyor
Semicoke cooler, pyrolysis furnace are connected with cracking Gas Cooler by pipeline, and the outlet for cracking cooler is sequentially connected by pipeline
There are separator and gas electricity generator, generator to be electrically connected with electrical appliance；Further include air blower, the air outlet of air blower, which is connected with, to be changed
Heat pipe, heat exchanger tube are connect after semicoke cooler and cracking Gas Cooler with the air inlet of dryer successively.
The utility model is utilized organic waste as resource, solves organic waste caused by environment
Pollution, while saving the land resource of organic waste occupancy.Cracking gas when being disposed to organic waste cracking passes through combustion
Gas generator carry out the direct generation of electricity, improve generating efficiency, avoid the secondary pollution caused by environment, prevent bioxin and
The generation of dust.
The utility model recycles the heat of pyrolysis product, is used for drying material, makes the heat generated in system
It is utilized effectively, reduces energy consumption.Also, when the heat to cracking gas exchanges heat, tar steam in cracking gas and
Vapor obtains condensation sedimentation, is purified to cracking gas, and cracking gas not containing water vapor and when tar steam, calorific value obtains
It significantly improves.After condensation separation, the calorific value of cracking gas reaches 14000kj/Nm3~16000kj/Nm3, and without cold
The calorific value of the cracking gas of solidifying separation is only 9000kj/Nm3~12000kj/Nm3.In the case where cracking gas calorific value raising, phase
Debirs energy conversion efficiency should be improved, tool has an unexpected effect.
Embodiment two
On the basis of embodiment one, the exhaust outlet of the generator is connected with waste heat boiler, waste heat boiler by pipeline
Steam (vapor) outlet and the air inlet of pyrolysis furnace connected by pipeline.The high temperature carbon dioxide and vapor that fuel gas buring generates are formed
High-temperature gas mixture stream, high-temperature gas mixture are streamed into waste heat boiler, are exchanged heat with the soft water in boiler, and soft water absorption heat becomes to steam
Vapour.Steam is transported to pyrolysis furnace, as packing inert gas, ensures the safety of pyrolysis furnace.To which the heat of fuel gas buring obtains
It efficiently uses, reduces the energy consumption of system.
Embodiment three
The feed inlet of the dryer is connected with the filter press for filter residue by screw conveyor.The row of the dryer
Gas port is connected with clarifier by pipeline.Clarifier can evolve to the tail gas being discharged in dryer, reduce pernicious gas
Discharge.
Example IV
On the basis of above-mentioned any one embodiment, a kind of electricity generation system of debirs clean utilization, including it is as follows
Step：
A) feed purification；Mechanical grading, removal are carried out to organic wastes such as excrement of animals, house refuses using filter press
The solid impurities such as the soil, brick, glass, stone, the iron filings that mix.
B) raw material drying：Purified debirs are transported to drying machine, processing is dried, then is granulated；It will
In the closed feeding dryer of raw material screw conveyor after purification process, with air blower send through semicoke cooler, cracking
The wind of Gas Cooler heating is in direct contact, and is dried.After the drying of organic waste materials drying machine, through sending secret to close feeding comminutor
It is inside granulated, particle organic waste is stored into material bin.
C) organic cracking：The organic granular material that step b) is obtained is placed in pyrolysis furnace, the temperature of pyrolysis furnace is controlled
At 500 DEG C~550 DEG C, organic granular material obtains the combustible gas mixture based on hydrogen and organic hydrocarbon and semicoke through cracking.
It uses water vapour to be used as inert gas in cracking feed and reaction process, completely cuts off air, while gas quantity can also be increased, and subtract
The purpose of few carbonized stock.
D) fuel gases calorific value and Waste Heat Reuse are improved：It is exchanged heat respectively to combustible gas mixture and semicoke using air,
Heated air be supplied to b) in drying machine.The utility model recycles the heat of pyrolysis product, for drying
Raw material makes the heat generated in system be utilized effectively, and reduces energy consumption.Also, it exchanges heat in the heat to cracking gas
When, tar steam and vapor in cracking gas obtain condensation sedimentation, to which cracking gas is purified, cracking gas not containing water vapor
When with tar steam, calorific value is improved significantly, and accordingly improves debirs energy conversion efficiency.
E) gas-purification：Air mixture made from step d) is subjected to purified treatment, it is made to react with lye, is removed
Sour gas in cracking gas obtains pure fuel gas；
F) fuel gas generation：Combustion gas is made in step d) to put into the cylinder body of gas electricity generator, combustion gas generates quick-fried in cylinder body
Fried and propelling gas turbine engine piston externally does work, and driving generator amature rotation realizes combustion gas to which mechanical energy is converted to electric energy
Turbine generates electricity.The exhaust gas that burning generates is outer after cooling recycling heat to be arranged.
The utility model is utilized organic waste as resource, solves organic waste caused by environment
Pollution, while saving the land resource of organic waste occupancy.Cracking gas when being disposed to organic waste cracking passes through combustion
Gas generator carry out the direct generation of electricity, improve generating efficiency, avoid the secondary pollution caused by environment, prevent bioxin and
The generation of dust.
The utility model reduces the discharge of harmful substance, reduces the pollution of environment.It is complete with the utility model technology
Face is promoted, and China will reduce flue dust object discharge capacity 980,000 tons of amounts, the sulfur dioxide object discharge capacitys 6,200,000 generated by power generation every year
Ton, 6,200,000 tons or so of nitrogen oxide emission.Meanwhile can handle every year more than 700,000,000 tons of existing stalk, 1,500,000 tons of excrement of animals,
1.5 hundred million tons of municipal refuse realizes that waste " renewable resource " is worth up to 25,000,000,000 yuan.
Claims (4)
1. a kind of electricity generation system of debirs clean utilization, which is characterized in that including dryer, dryer passes through helical feed
Machine is connected with comminutor, and comminutor is connected with pyrolysis furnace by belt conveyor；Pyrolysis furnace is connected with half by screw conveyor
Burnt cooler, pyrolysis furnace are connected with cracking Gas Cooler by pipeline, and the outlet for cracking cooler is connected in turn by pipeline
Separator and gas electricity generator；Further include air blower, the air outlet of air blower is connected with heat exchanger tube, and heat exchanger tube passes through semicoke successively
It is connect with the air inlet of dryer after cooler and cracking Gas Cooler.
2. a kind of electricity generation system of debirs clean utilization according to claim 1, which is characterized in that the generator
Exhaust outlet waste heat boiler is connected with by pipeline, the steam (vapor) outlet of waste heat boiler and the air inlet of pyrolysis furnace are connected by pipeline
It connects.
3. a kind of electricity generation system of debirs clean utilization according to claim 1, which is characterized in that the dryer
Feed inlet the filter press for filter residue is connected with by screw conveyor.
4. a kind of electricity generation system of debirs clean utilization according to claim 1, which is characterized in that the dryer
Exhaust outlet clarifier is connected with by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721593886.0U CN207756595U (en) | 2017-11-24 | 2017-11-24 | A kind of electricity generation system of debirs clean utilization |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721593886.0U CN207756595U (en) | 2017-11-24 | 2017-11-24 | A kind of electricity generation system of debirs clean utilization |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207756595U true CN207756595U (en) | 2018-08-24 |
Family
ID=63189136
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721593886.0U Active CN207756595U (en) | 2017-11-24 | 2017-11-24 | A kind of electricity generation system of debirs clean utilization |
Country Status (1)
| Country | Link |
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| CN (1) | CN207756595U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110404926A (en) * | 2019-07-05 | 2019-11-05 | 上海齐耀热能工程有限公司 | A kind of corona treatment organic waste system |
| CN112077131A (en) * | 2020-10-29 | 2020-12-15 | 内蒙古蒙投环境股份有限公司 | Continuous carbonization and pyrolysis system for municipal solid waste |
-
2017
- 2017-11-24 CN CN201721593886.0U patent/CN207756595U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110404926A (en) * | 2019-07-05 | 2019-11-05 | 上海齐耀热能工程有限公司 | A kind of corona treatment organic waste system |
| CN110404926B (en) * | 2019-07-05 | 2024-04-12 | 上海齐耀热能工程有限公司 | System for treating organic waste by plasma |
| CN112077131A (en) * | 2020-10-29 | 2020-12-15 | 内蒙古蒙投环境股份有限公司 | Continuous carbonization and pyrolysis system for municipal solid waste |
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