CN105885954A - Combustible refuse gasifying power generation system - Google Patents
Combustible refuse gasifying power generation system Download PDFInfo
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- CN105885954A CN105885954A CN201410850106.0A CN201410850106A CN105885954A CN 105885954 A CN105885954 A CN 105885954A CN 201410850106 A CN201410850106 A CN 201410850106A CN 105885954 A CN105885954 A CN 105885954A
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- gas
- decoking
- grades
- gasification furnace
- decoking device
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- 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
- Y02T10/30—Use of alternative fuels, e.g. biofuels
Abstract
The invention discloses a combustible refuse gasifying power generation system which comprises a feeding system, a gasifier (3), a dust removal system, a decoking system and a drying system. The feeding system, the gasifier (3), the dust removal system, the decoking system and the drying system are sequentially connected. A water sealing flame arrester (20) is mounted between the decoking system and the drying system. The refuse anaerobic pyrolysing and gasifying technology is adopted, all industrial (household) combustible refuse is converted into combustible gas free of dioxin through low-temperature pyrolysing and gasifying, the gas is supplied to a gas power generation unit for power generation after being subjected to dust removal and decoking, and therefore high-grade energy can be obtained from low-grade energy; the derivative product tar of the gas can be processed to be extracted to form high-quality diesel oil or chemical products, waste is turned into wealth, environmental production is achieved, energy is saved, and especially the problem of refuse treatment is solved.
Description
Technical field
The present invention relates to field of environment protection, particularly to a kind of inflammable refuse gasification generating be
System.
Background technology
Due to the raising of process of industrialization, the thing followed is that industrial refuse is also in substantial amounts of increasing
Long, and become again pollution environment, polluted water resources, the hidden danger of harm human survival.One
Directly burning away the refuse in a little countries, produces substantial amounts of containing the two carcinogenic gases of English, more
Exacerbate people and talk rubbish complexion changed atmosphere.
Summary of the invention
(1) to solve the technical problem that
The problem to be solved in the present invention is to provide a kind of inflammable refuse gasification electricity generation system, to overcome
Defect of the prior art.
(2) technical scheme
For reaching above-mentioned purpose, the present invention provides a kind of inflammable refuse gasification electricity generation system, bag
Include feeding system, gasification furnace 3, dust pelletizing system, decoking system and drying system；Described feeding
System, gasification furnace 4, dust pelletizing system, decoking system and drying system be sequentially connected；Described
Decoking system and drying system successively between water seal fire arrestor 20 is installed；
Described feeding system includes elevating hopper 1, elevating hopper wheel frame 2, hoist engine 4, steel wire
Rope 5 and fixed pulley 6, described elevating hopper 1 is at described hoist engine 4, steel wire rope 5 and fixed pulley
It is transported to top along described elevating hopper wheel frame 2 from bottom, by described gasification furnace under 6 effects
In the material receiving port at the top of 3 delivers to described gasification furnace 3 and fully fire in described gasification furnace 3
Burn；
Described dust pelletizing system includes one cyclonic cleaner unit 7 and second cyclone dust extractor 8, described
One cyclonic cleaner unit 7 is connected with second cyclone dust extractor 8；Described one cyclonic cleaner unit 7
It is connected with described gasification furnace 3, for by larger volume in described gasification furnace 3 expellant gas
Dust remove；Described second cyclone dust extractor 8, is used for removing smaller size smaller in residual gas
Dust and tar；
Described decoking system include condenser 9,10, three grades of whirlwind decoking devices 11 of oil strain blower fan,
Water-bath spraying goes out cleaner unit 12,13, two grades of oil water separators 14, of primary oil water separator
Level spray decoking device 15, two grades spray decoking device 16, Category Four cyclone decoking device 17, high pressure draw
Blower fan 18 and five-stage whirlwind decoking device 19, described condenser 9, oil strain blower fan 10, three grades rotation
Wind decoking device 11, water-bath spraying go out cleaner unit 12,13, two grades of profits of primary oil water separator
Separator 14, one-level spray decoking device 15, two grades spray decoking device 16, Category Four cyclone decoking
Device 17, high-pressure suction fan 18 and five-stage whirlwind decoking device 19 are sequentially connected；
Described condenser 9, makes the tar cooling liquid produced in described gas；
Described drying system includes one-level exsiccator 21, secondary drying device 22, fluid seal gas holder
24 and gas-liquid separator 26, described one-level exsiccator 21, secondary drying device 22, wet type are stored up
Gas holder 24 and gas-liquid separator 26 are sequentially connected；
Described electricity generation system also includes generating set 27, water circulating pump 28, hydraulic power unit 29
With smoke of gunpowder gas wash tower 30；
Garbage fuel at described gasification furnace 4 through cold drying-cracking-oxidation-reduction, generation
Fuel gas is drawn from described gasification furnace 4 bottom under the effect of oil strain blower fan 10, thus enters
Enter in described one cyclonic cleaner unit 7；
Described fuel gas through described three grades of whirlwind decoking devices 11, drench cleaner unit 12, one-level
13, two grades of oil water separators 14 of oil water separator, one-level spray decoking device 15, two grades spray
Decoking device 16, Category Four cyclone decoking device 17, high-pressure suction fan 18, five-stage whirlwind decoking device
19, water seal fire arrestor 20, one-level exsiccator 21, secondary drying device 22, fluid seal gas holder
24 and gas-liquid separator 26 purified treatment after remove the moisture in gas and tar, finally enter
Internal combustion engine generator group 27 is directly done work generating.
Further, it is connected with described hydraulic power unit 29 bottom described gasification furnace 3, top and institute
State smoke of gunpowder gas wash tower 30 to be connected.
Further, described gasification furnace 3 is additionally provided with lighting-up tuyere, gas outlet and ash hole, institute
Stating combustiblerefuse fuel to be lighted by described lighting-up tuyere, the gas produced after burning is by described
Gas outlet enters described one cyclonic cleaner unit 7；The dust stratification produced after burning, by described gas
Change the stove coral within stove 3 and unload grey to furnace bottom, described ash hole draw off.
Further, described hydraulic power unit 29 controls the unlatching Guan Bi of described stove coral.
Further, it is all provided with bottom described one cyclonic cleaner unit 7 and second cyclone dust extractor 8
There is dust mouth.
Further, 9, three grades of whirlwind decoking devices 11, Category Four cyclone decoking devices of described condenser
17, five-stage whirlwind decoking device 19, water seal fire arrestor 20, one-level exsiccator 21, secondary drying
It is equipped with coke outlet bottom device 22 and gas-liquid separator 26.
Further, it is provided with between described fluid seal gas holder 24 and described gas-liquid separator 26
Effusion meter 25, described effusion meter 25 for read the flow entering generating set 27 combustion gas and
Gaseous-pressure.
Further, described water circulating pump 28 respectively with described water bath spraying duster 12, one-level
Spray decoking device 15 is connected with two grades of spray decoking devices 16.
Further, described water-bath spraying goes out cleaner unit 12, primary oil water separator 13, two grades
It is all provided with bottom oil water separator 14, one-level spray decoking device 15 and two grades of spray decoking devices 16
There are coke outlet and outlet.
(3) beneficial effect
Compared with prior art, technical scheme has the advantage that and utilizes rubbish to detest
Oxygen cracking gasification technology, gasifies various industry (in life) combustiblerefuse through low temperature pyrolyzer
Be converted to the fuel gas without two English, by these gases after dedusting devokes, supply combustion
Gas generating set generates electricity, and reaches to obtain high-grade energy from low-grade energy, its derivative product
Product tar can be refined into diesel oil or the chemical products of high-quality through processing, turn waste into wealth, i.e.
Protection environment, saves again the energy, has especially captured a difficult problem for garbage disposal.
Accompanying drawing explanation
Fig. 1 a to Fig. 1 c is the structural representation of the present invention a kind of inflammable refuse gasification electricity generation system；
Fig. 2 is the enlarged drawing of the aminoacyl site in Fig. 1 b；
Fig. 3 is the schematic diagram of the effusion meter of the inflammable refuse gasification electricity generation system of the present invention.
Detailed description of the invention
Below in conjunction with the accompanying drawings and embodiment, the detailed description of the invention of the present invention is made the most in detail
Describe.Following example are used for illustrating the present invention, but are not limited to the scope of the present invention.
The structure of the inflammable refuse gasification electricity generation system of the present invention, as shown in Fig. 1 a to Fig. 3, is wrapped
Include feeding system, gasification furnace 3, dust pelletizing system, decoking system and drying system；Described feeding
System, gasification furnace 4, dust pelletizing system, decoking system and drying system be sequentially connected；Described
Decoking system and drying system successively between water seal fire arrestor 20 is installed；
Described feeding system includes elevating hopper 1, elevating hopper wheel frame 2, hoist engine 4, steel wire
Rope 5 and fixed pulley 6, described elevating hopper 1 is at described hoist engine 4, steel wire rope 5 and fixed pulley
It is transported to top along described elevating hopper wheel frame 2 from bottom, by described gasification furnace under 6 effects
In the material receiving port at the top of 3 delivers to described gasification furnace 3 and fully fire in described gasification furnace 3
Burn；
Described dust pelletizing system includes one cyclonic cleaner unit 7 and second cyclone dust extractor 8, described
One cyclonic cleaner unit 7 is connected with second cyclone dust extractor 8；Described one cyclonic cleaner unit 7
It is connected with described gasification furnace 3, for by larger volume in described gasification furnace 3 expellant gas
Dust remove；Described second cyclone dust extractor 8, is used for removing smaller size smaller in residual gas
Dust and tar；
Described decoking system include condenser 9,10, three grades of whirlwind decoking devices 11 of oil strain blower fan,
Water-bath spraying goes out cleaner unit 12,13, two grades of oil water separators 14, of primary oil water separator
Level spray decoking device 15, two grades spray decoking device 16, Category Four cyclone decoking device 17, high pressure draw
Blower fan 18 and five-stage whirlwind decoking device 19, described condenser 9, oil strain blower fan 10, three grades rotation
Wind decoking device 11, water-bath spraying go out cleaner unit 12,13, two grades of profits of primary oil water separator
Separator 14, one-level spray decoking device 15, two grades spray decoking device 16, Category Four cyclone decoking
Device 17, high-pressure suction fan 18 and five-stage whirlwind decoking device 19 are sequentially connected；
Described condenser 9, makes the tar cooling liquid produced in described gas；
Described drying system includes one-level exsiccator 21, secondary drying device 22, fluid seal gas holder
24 and gas-liquid separator 26, described one-level exsiccator 21, secondary drying device 22, wet type are stored up
Gas holder 24 and gas-liquid separator 26 are sequentially connected；
Described electricity generation system also includes generating set 27, water circulating pump 28, hydraulic power unit 29
With smoke of gunpowder gas wash tower 30；
Garbage fuel at described gasification furnace 4 through cold drying-cracking-oxidation-reduction, generation
Fuel gas is drawn from described gasification furnace 4 bottom under the effect of oil strain blower fan 10, thus enters
Enter in described one cyclonic cleaner unit 7；
Described fuel gas through described three grades of whirlwind decoking devices 11, drench cleaner unit 12, one-level
13, two grades of oil water separators 14 of oil water separator, one-level spray decoking device 15, two grades spray
Decoking device 16, Category Four cyclone decoking device 17, high-pressure suction fan 18, five-stage whirlwind decoking device
19, water seal fire arrestor 20, one-level exsiccator 21, secondary drying device 22, fluid seal gas holder
24 and gas-liquid separator 26 purified treatment after remove the moisture in gas and tar, finally enter
Internal combustion engine generator group 27 is directly done work generating.
Being connected with described hydraulic power unit 29 bottom described gasification furnace 3, top is removed with the described smoke of gunpowder
Chimney 30 is connected.
Lighting-up tuyere, gas outlet and ash hole, described flammable rubbish it is additionally provided with on described gasification furnace 3
Rubbish fuel is lighted by described lighting-up tuyere, and the gas produced after burning is entered by described gas outlet
Enter described one cyclonic cleaner unit 7；The dust stratification produced after burning, by described gasification furnace 3
Internal stove coral unloads ash and arrives furnace bottom, described ash hole draw off.
Described hydraulic power unit 29 controls the unlatching Guan Bi of described stove coral.
It is equipped with dust mouth bottom described one cyclonic cleaner unit 7 and second cyclone dust extractor 8.
Described condenser 9, three grades of whirlwind decoking devices 11, Category Four cyclone decoking device 17, Pyatyis
Whirlwind decoking device 19, water seal fire arrestor 20, one-level exsiccator 21, secondary drying device 22 and
It is equipped with coke outlet bottom gas-liquid separator 26.
Between described fluid seal gas holder 24 and described gas-liquid separator 26, effusion meter 25 is installed,
Described effusion meter 25 is for reading the flow and gaseous-pressure entering generating set 27 combustion gas.
Described water circulating pump 28 devokes with described water bath spraying duster 12, one-level spray respectively
Device 15 is connected with two grades of spray decoking devices 16.
Described water-bath spraying goes out cleaner unit 12,13, the two grades of oil-water separation of primary oil water separator
It is equipped with coke outlet bottom device 14, one-level spray decoking device 15 and two grades of spray decoking devices 16
And outlet.
Specific implementation process:
Under hoist engine 4, steel wire rope 5, fixed pulley 6 control, elevating hopper 1 is led along elevating hopper
The combustiblerefuse fuel material receiving port from gasification furnace 3 top is delivered in gasification furnace 3 by wheel carrier 2,
Garbage fuel in gasification furnace 3 through links such as cold drying-cracking-oxidation-reduction, flammable
Solid waste gas is drawn from lower portion of furnace body under the effect of oil strain blower fan 10.
Through one cyclonic dedusting 7, removing large volume of dust in gas, efficiency is
70-85%.Two grades of cyclone dust removals 8, remove dust and the part tar of smaller size smaller in gas,
Efficiency 85-90%.
Condenser 9, plays cooling decoking effect, by coal-tar middle oil for combustion gas cooling liquefaction.
Through three grades of whirlwind decoking devices 11, water bath spraying duster 12, primary oil water separator 13,
Two grades of oil water separators 14, one-level spray decoking device 15, two grades spray decoking device 16, level Four
Whirlwind decoking device 17, high-pressure suction fan 18, five-stage whirlwind decoking device 19, water seal fire arrestor
20, after one-level exsiccator 21, secondary drying device 22 and gas-liquid separator 26 purified treatment,
Removing the moisture in gas and tar, qualified combustion gas enters internal combustion under certain pressure effect
Generating set 27 directly does work generating.After fuel gas buring acting, discharge from electromotor smoke exhaust pipe,
Discharge reaches EU criteria.
Gasification furnace after a period of operation, has a certain amount of dust stratification, at this moment opens hydraulic pressure in stove
Pumping plant 29, action stove coral unloads ash and arrives furnace bottom, drawn off by after ash hole to wind stopping device, and packing is received
Deposit.
All ash discharges and oil extraction are all received and kept with special container.
During slagging tap, do not affect aerogenesis, the compact coordination of whole production procedure, no pressure
And other harm.
Flow and the gaseous-pressure entering generating set combustion gas is read by effusion meter 25.
Described fluid seal gas holder 24, for the offer combustion gas deposit that works continuously for generating set 27,
The air inlet of described fluid seal gas holder 24 and two ends of giving vent to anger are separately installed with check-valves 23, to ensure fortune
The safety of combustion gas in row.
Follow used by water bath spraying duster 12, spray grease trap 15, spray deduster 16
Ring water is provided by water circulating pump 28.
When maintenance down, part of fuel in gasification furnace, may be had not gasify to the greatest extent.Thus have non-
Combustible fumes produces, and adds Tower for eliminating smoke and dust 30 and gives smoke-eliminating purifying.Whole system is begun
It is in the state of environment-friendly type eventually.Advantages of the present invention:
(1) raw material easily collecting, at the bottom of cost；
(2) simple to operation safe and reliable；Aerogenesis generating is not affected while charging, ash discharge,
Reach timeless and continue aerogenesis；
(3) gas tar oil content is low；Use cracking technique in stove, make in combustiblerefuse cracking process
The tar of more than 90% cracks in stove, i.e. improves fuel gases calorific value and eliminates again tar pair
The secondary pollution of surrounding enviroment.Use dry ash removal technology, it is achieved that free from dust, without sewage row
The target put；
(4) advanced technology, thermal conversion efficiency is up to 75-80%；
(5) compact conformation, it is convenient to start, and aerogenesis is fast；Belong to the most pioneering, every technology
Index reaches domestically leading level.
The present invention utilizes rubbish anaerobism to crack gasification technology, flammable for various industry (in life)
Rubbish is converted to the fuel gas without two English, by these gas warps through low temperature pyrolyzer gasification
After crossing dedusting decoking, supply jet dynamic control generates electricity, and reaches to obtain from low-grade energy
High-grade energy, its derived product tar can be refined into diesel oil or the change of high-quality through processing
Chemical product, turns waste into wealth, and i.e. protects environment, saves again the energy, has especially captured garbage disposal
A difficult problem.
The above is only the preferred embodiment of the present invention, it is noted that lead for this technology
For the those of ordinary skill in territory, on the premise of without departing from the technology of the present invention principle, it is also possible to
Making some improvements and modifications, these improvements and modifications also should be regarded as protection scope of the present invention.
Claims (9)
1. an inflammable refuse gasification electricity generation system, it is characterised in that include feeding system,
Gasification furnace (3), dust pelletizing system, decoking system and drying system；Described feeding system, gas
Change stove (4), dust pelletizing system, decoking system and drying system be sequentially connected；Described decoking system
System and drying system successively between water seal fire arrestor (20) is installed；
Described feeding system include elevating hopper (1), elevating hopper wheel frame (2), hoist engine (4),
Steel wire rope (5) and fixed pulley (6), described elevating hopper (1) described hoist engine (4),
Along described elevating hopper wheel frame (2) from bottom under steel wire rope (5) and fixed pulley (6) effect
It is transported to top, delivers to described gasification furnace by the material receiving port at the top of described gasification furnace (3)
(3) in and fully burn in described gasification furnace (3)；
Described dust pelletizing system includes one cyclonic cleaner unit (7) and second cyclone dust extractor (8),
Described one cyclonic cleaner unit (7) is connected with second cyclone dust extractor (8)；Described one-level
Cyclone dust extractor (7) is connected with described gasification furnace (3), for by described gasification furnace (3)
In expellant gas, large volume of dust removes；Described second cyclone dust extractor (8), uses
In dust and the tar of removing smaller size smaller in residual gas；
Described decoking system includes condenser (9), oil strain blower fan (10), three grades of whirlwind decokings
Device (11), water-bath spraying go out cleaner unit (12), primary oil water separator (13), two grades of oil
Water separator (14), one-level spray decoking device (15), two grades spray decoking device (16), four
Level whirlwind decoking device (17), high-pressure suction fan (18) and five-stage whirlwind decoking device (19),
Described condenser (9), oil strain blower fan (10), three grades of whirlwind decoking devices (11), water-bath sprays
Drench cleaner unit (12), primary oil water separator (13), two grades of oil water separators (14),
One-level spray decoking device (15), two grades spray decoking device (16), Category Four cyclone decoking device (17),
High-pressure suction fan (18) and five-stage whirlwind decoking device (19) are sequentially connected；
Described condenser (9), makes the tar cooling liquid produced in described gas；
Described drying system includes one-level exsiccator (21), secondary drying device (22), wet type
Gas storage holder (24) and gas-liquid separator (26), described one-level exsiccator (21), two grades do
Dry device (22), fluid seal gas holder (24) and gas-liquid separator (26) are sequentially connected；
Described electricity generation system also includes generating set (27), water circulating pump (28), hydraulic pump
Stand (29) and smoke of gunpowder gas wash tower (30)；
Garbage fuel, produces through cold drying-cracking-oxidation-reduction at described gasification furnace (4)
Fuel gas draw from described gasification furnace (4) bottom under the effect of oil strain blower fan (10)
Go out, hence in described one cyclonic cleaner unit (7)；
Described fuel gas through described three grades of whirlwind decoking devices (11), drench cleaner unit (12),
Primary oil water separator (13), two grades of oil water separators (14), one-level spray decoking device (15),
Two grades spray decoking device (16), Category Four cyclone decoking device (17), high-pressure suction fan (18),
Five-stage whirlwind decoking device (19), water seal fire arrestor (20), one-level exsiccator (21), two grades
Remove after exsiccator (22), fluid seal gas holder (24) and gas-liquid separator (26) purified treatment
Remove the moisture in gas and tar, finally enter internal combustion engine generator group (27) directly acting and send out
Electricity.
Inflammable refuse gasification electricity generation system the most according to claim 1, it is characterised in that
Described gasification furnace (3) bottom is connected with described hydraulic power unit (29), top and the described smoke of gunpowder
Gas wash tower (30) is connected.
Inflammable refuse gasification electricity generation system the most according to claim 2, it is characterised in that
Lighting-up tuyere, gas outlet and ash hole, described combustiblerefuse it is additionally provided with on described gasification furnace (3)
Fuel is lighted by described lighting-up tuyere, and the gas produced after burning is entered by described gas outlet
Described one cyclonic cleaner unit (7)；The dust stratification produced after burning, by described gasification furnace (3)
Internal stove coral unloads ash and arrives furnace bottom, described ash hole draw off.
Inflammable refuse gasification electricity generation system the most according to claim 3, it is characterised in that
Described hydraulic power unit 29 controls the unlatching Guan Bi of described stove coral.
Inflammable refuse gasification electricity generation system the most according to claim 4, it is characterised in that
Described one cyclonic cleaner unit (7) and second cyclone dust extractor (8) bottom are equipped with out dirt
Mouthful.
Inflammable refuse gasification electricity generation system the most according to claim 5, it is characterised in that
Described condenser (9), three grades of whirlwind decoking devices (11), Category Four cyclone decoking device (17), five
Level whirlwind decoking device (19), water seal fire arrestor (20), one-level exsiccator (21), two grades do
Dry device (22) and gas-liquid separator (26) bottom are equipped with coke outlet.
Inflammable refuse gasification electricity generation system the most according to claim 6, it is characterised in that
Between described fluid seal gas holder (24) and described gas-liquid separator (26), effusion meter is installed
(25), described effusion meter (25) is used for reading the flow entering generating set (27) combustion gas
And gaseous-pressure.
Inflammable refuse gasification electricity generation system the most according to claim 7, it is characterised in that
Described water circulating pump (28) removes with described water bath spraying duster (12), one-level spray respectively
Burnt device (15) is connected with two grades of sprays decoking device (16).
9. according to the inflammable refuse gasification electricity generation system described in any one of claim 1 to 8,
It is characterized in that, described water-bath spraying go out cleaner unit (12), primary oil water separator (13),
Two grades of oil water separators (14), one-levels spray decoking device (15) and two grades of sprays decoking device (16)
Bottom is equipped with coke outlet and outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410850106.0A CN105885954A (en) | 2014-12-31 | 2014-12-31 | Combustible refuse gasifying power generation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410850106.0A CN105885954A (en) | 2014-12-31 | 2014-12-31 | Combustible refuse gasifying power generation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105885954A true CN105885954A (en) | 2016-08-24 |
Family
ID=56700848
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410850106.0A Pending CN105885954A (en) | 2014-12-31 | 2014-12-31 | Combustible refuse gasifying power generation system |
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| CN (1) | CN105885954A (en) |
Citations (6)
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|---|---|---|---|---|
| CN1661278A (en) * | 2004-02-25 | 2005-08-31 | 江苏正昌集团有限公司 | Technique for generating electricity through gasifying ramification of garbage |
| CN1916495A (en) * | 2006-07-24 | 2007-02-21 | 王玉志 | Environmental protection, energy sources recovery type garbage treatment equipment |
| CN102816578A (en) * | 2012-07-16 | 2012-12-12 | 严大春 | Method for integrative sorting and destructive distillation pyrolysis and gasification of household refuse without discharge of dioxin |
| CN202883121U (en) * | 2012-11-05 | 2013-04-17 | 山东省南郊集团环保节能股份有限公司 | Industrial combustible gas generating system |
| CN103242134A (en) * | 2013-04-25 | 2013-08-14 | 深圳市炬能生物质气化科技有限公司 | Pyrolysis gasification and purification method of household garbage |
| CN203924730U (en) * | 2013-06-25 | 2014-11-05 | 程辉 | Energy-efficient integrated stepped type concrete dry is wet from batch mixing pulp shooting machine |
-
2014
- 2014-12-31 CN CN201410850106.0A patent/CN105885954A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1661278A (en) * | 2004-02-25 | 2005-08-31 | 江苏正昌集团有限公司 | Technique for generating electricity through gasifying ramification of garbage |
| CN1916495A (en) * | 2006-07-24 | 2007-02-21 | 王玉志 | Environmental protection, energy sources recovery type garbage treatment equipment |
| CN102816578A (en) * | 2012-07-16 | 2012-12-12 | 严大春 | Method for integrative sorting and destructive distillation pyrolysis and gasification of household refuse without discharge of dioxin |
| CN202883121U (en) * | 2012-11-05 | 2013-04-17 | 山东省南郊集团环保节能股份有限公司 | Industrial combustible gas generating system |
| CN103242134A (en) * | 2013-04-25 | 2013-08-14 | 深圳市炬能生物质气化科技有限公司 | Pyrolysis gasification and purification method of household garbage |
| CN203924730U (en) * | 2013-06-25 | 2014-11-05 | 程辉 | Energy-efficient integrated stepped type concrete dry is wet from batch mixing pulp shooting machine |
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