CN102517092B - Counter combustion-type pyrolysis gasification equipment for biomass waste resources - Google Patents
Counter combustion-type pyrolysis gasification equipment for biomass waste resources Download PDFInfo
- Publication number
- CN102517092B CN102517092B CN201110420412.7A CN201110420412A CN102517092B CN 102517092 B CN102517092 B CN 102517092B CN 201110420412 A CN201110420412 A CN 201110420412A CN 102517092 B CN102517092 B CN 102517092B
- Authority
- CN
- China
- Prior art keywords
- biological
- chamber
- communicated
- heat exchange
- outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The invention relates to counter combustion-type pyrolysis gasification equipment for biomass waste resources, which comprises a counter burning-type gasification furnace and a high-temperature biological mixed gas separator. A chimney is arranged at the top part of a gas flow buffer chamber at the upper part of a heat exchange chamber between a bunker and the inner wall of a furnace body; heat exchange pipes of the heat exchange chamber are communicated with the gas flow buffer chamber and a combustor at the bottom part of the furnace body. Both ends of heat exchange pipes in a heat transfer chamber of the high-temperature biological mixed gas separator are respectively communicated with a biological gas outlet and a biological mixed liquor outlet; the bottom ends of the heat exchange pipes are communicated with the chimney; a static separating chamber is divided into a left chamber and a right chamber by a partition plate, wherein the lower parts of the left chamber and the right chamber are communicated; a biological light tar outlet is arranged above the side wall of one of the two chambers provided with a biological mixed liquor inlet; a biological acetic acid outlet is arranged above the side wall of the other chamber; and the bottom part of the static separating chamber is provided with a biological heavy tar outlet. Agricultural wastes are converted into biological combustible gas, biological tar, biological acetic acid and hot water which are used for living and production of rural residents, and secondary pollution and the wastes of secondary transformation resources in the transformation process are eliminated.
Description
Technical field
The present invention relates to a kind of pyrolysis converting apparatus of biomass waste resource, a kind ofly specifically take agricultural crop straw as main counter combustion-type pyrolysis gasification equipment for biomass waste resources.
Background technology
China Shi Yige large agricultural country has produced the biomass resources such as a large amount of agricultural crop straws, chaff slag in agriculture production and processing of farm products.Traditional utilizes mode mainly as home energy source, feed, fertilizer, industrial raw material and material of construction.Fast development along with agrotechnique modernization and rural economy, life in the countryside level significantly improves and the sudden change of the mode of production of living, rural households select the ratio of commercial energy resource improving constantly, quantity by agricultural crop straw as the energy constantly declines, and commercial energy resource (as coal, liquefied gas etc.) has become main cooking energy.Cultivation institute is in order to biomass straw, and weeds feed is substituted by commercial feed, and the required biomass organic fertilizer of agriculture production is substituted by inorganic fertilizer, and life of farmers and agriculture production stalk used sharply declines.Meanwhile, agricultural crop straw output is with farm crop, particularly the increase of food crop output and increasing rapidly.Drug on the market causes that stalk is abandoned in field, house courtyard for agricultural crop straw, even in field, directly burned.Abandonment can affect environment and initiation fire at the stalk in house courtyard and field, causes pollution of waterhead.Crop straw burning can polluted air in the open, harm people ' s health, especially on airport, near Highway burning can affect traffic safety, causes the aircraft grounding, car tracing cauda collision, shade tree such as is burnt at the adverse consequences.At present, although various places government has all put into effect the rules of forbidding Open Burning Crop Residue, open incineration agricultural crop straw still remains incessant after repeated prohibition, and environment causes severe contamination, to society, causes tremendous economic loss.
When the biomass resources such as stalk are wasted; the current main fossil energy such as the combustion gas of using in China's industrial and agricultural production, fuel oil, heat energy, coal, oil reduces day by day; famine; energy dilemma has become the bottleneck problem of social development, is current problem in the urgent need to address.
China has a large population and a few land, particularly the arable land of agricultural has approached red line.In agriculture production because a large amount of agricultural chemicals, inorganic fertilizer are by life-time service, reaching prevention and elimination of disease and pests, improve the object of grain yield.Due to the life-time service of agricultural chemicals, inorganic fertilizer, utilization ratio is low, causes residual in soil and farm crop.Cause soil, water source, grain, vegetables, fruit to pollute.Pesticide residue in grain, vegetables, fruit have jeopardized health of human body safety, affect the raising of life in the countryside level and quality.
Along with social fast development, people more and more add attention for energy-saving and emission-reduction and ecological environmental protection, constantly seek to use the new energy, control atmosphere pollution, and energy-saving and emission-reduction, reduce Greenhouse effect.The technology that is comprehensively converted into available stock with biomass waste resources such as agricultural crop straw, ight soil, chaff slags has caused showing great attention to of departments at different levels of government.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of counter combustion-type pyrolysis gasification equipment for biomass waste resources, adopt trans burning, pyrolytic gasification technology, make biomass waste resource pyrolytic gasification under oxygen debt condition, change into biological inflammable gas, biological tar, biological acetic acid and hot water, and realize automatic feeding.
The present invention solves the problems of the technologies described above adopted technical scheme to be: a kind of counter combustion-type pyrolysis gasification equipment for biomass waste resources, comprise counter-burning type vapourizing furnace and high-temperature biological mixed gas separator, in the body of heater of counter-burning type vapourizing furnace, be provided with a vertical feed bin, between feed bin and the inwall of body of heater, be provided with heat exchange chamber, heat exchange chamber top is provided with air-flow buffer chamber, the top of air-flow buffer chamber is provided with the chimney being communicated with high-temperature biological mixed gas separator, the top of feed bin is provided with feed bin lid, the bottom of feed bin is pyrolysis chamber, between pyrolysis chamber and the combustion chamber of bottom of furnace body, be provided with fire grate, between the bottom of heat exchange chamber and combustion chamber, be provided with ignition channel, ignition channel is communicated with pyrolysis chamber with the lighting-up tuyere on furnace body wall, in heat exchange chamber, be provided with heat exchanger tube, one end of heat exchanger tube is communicated with air-flow buffer chamber, the other end is communicated with combustion chamber through ignition channel, on heat exchange chamber sidewall, be respectively equipped with water-in and water outlet.
Described high-temperature biological mixed gas separator is provided with housing, in housing, be provided with Heat Room and standing separation chamber, Heat Room is arranged on top, standing separation chamber, in Heat Room, be provided with snakelike or volution or rectilinear heat transfer tube, the sidewall of Heat Room is provided with heat exchange water import and heat exchange water outlet, the top of Heat Room is provided with biological flue gas outlet, bottom is provided with biological mixture export, the two ends of heat transfer tube are communicated with biological flue gas outlet and biological mixture export respectively, the bottom of heat transfer tube is communicated with the chimney of counter-burning type vapourizing furnace by the high-temperature biological mixed gas import arranging in housing sidewall, the biological mixture export of Heat Room is communicated with the biological mixed solution import at the top of standing separation chamber, at the indoor dividing plate that is provided with of standing separation, dividing plate is divided into two chambers in left and right by standing separation chamber, the bottom of two chambers is communicated with, biological mixed solution import is positioned at one of them chamber top, above the chamber sidewall that is provided with biological mixed solution import, be provided with biological tar light oil outlet, the sidewall top of another chamber is provided with biological acetic acid outlet, in the bottom of standing separation chamber, be provided with biological tar heavy oil outlet.
Described water-in is arranged on the lower sidewall of heat exchange chamber, and water outlet is arranged on the side wall upper part of heat exchange chamber.
Described lower portion of furnace body is provided with the ash output hole being communicated with combustion chamber.
Described housing is provided with thermal insulation layer.
The biological mixture export of described Heat Room is communicated to the biological mixed solution import at top, standing separation chamber by conduction pipe, high-temperature biological mixed gas import is communicated with conduction pipe.
Described high-temperature biological mixed gas import is connected with cleaning apparatus.
The setting position of described biological tar light oil outlet exports higher than biological acetic acid.
Described case top is provided with upper cover, and bottom is provided with lower cover, biological flue gas outlet and the outlet of biological tar heavy oil be separately positioned on upper cover with under cover.
The invention has the beneficial effects as follows: utilize counter combustion-type pyrolysis gasification equipment for biomass waste resources, agricultural wastes are converted into biological inflammable gas, biological tar, biological acetic acid and hot water.Biological inflammable gas is for resident's cooking; Biological acetic acid is used for bio-organic fertilizer processed, biology feed additive, Biocidal (bacterium) agent; Biological tar is used for Biocidal processed (bacterium) agent or biogas (bavin) oil.For urban residents' life and production.The pollution problem that the ight soil of solution crop straw burning, chemical fertilizer life-time service, intensive culture causes, improves agroecological environment; Solve urban residents and live with energy, change lifestyles; Reduce agriculture production fertilizer application amount improvement Soil structure, improve quality of agricultural product.Counter combustion-type pyrolysis gasification equipment for biomass waste resources, in combustion processes, fuel reduces gradually and forms hole, and the fuel in feed bin moves down under self gravitation effect, automatically fills up hole, implements automatic feeding and reduces labour intensity.Simple in structure, multiple functional, equipment maintenance cost and low cost of manufacture, thereby can significantly reduce running cost, increase economic efficiency, in the practicality of using and cost benefit, meet the current structure of agricultural production and rural economic development required, quite there is industry development and application value.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Fig. 2 is the structural representation of counter-burning type vapourizing furnace.
Fig. 3 is the set-up mode schematic diagram of heat exchange chamber in counter-burning type vapourizing furnace.
Fig. 4 is the structural representation of high-temperature biological mixed gas separator.
Mark in figure: 1, counter-burning type vapourizing furnace, 101, body of heater, 1011, ash output hole, 102, feed bin, 1021, feed bin lid, 1022, pyrolysis chamber, 103, heat exchange chamber, 1031, water-in, 1032, water outlet, 104, air-flow buffer chamber, 105, chimney, 106, combustion chamber, 107, fire grate, 108, ignition channel, 1081, lighting-up tuyere, 109, heat exchanger tube, 2, high-temperature biological mixed gas separator, 201, housing, 2011, high-temperature biological mixed gas import, 2012, upper cover, 2013, lower cover, 202, Heat Room, 2021, heat exchange water import, 2022, heat exchange water outlet, 203, standing separation chamber, 2031, biological mixed solution import, 2032, biological tar light oil outlet, 2033, biological acetic acid outlet, 2034, biological tar heavy oil outlet, 204, heat transfer tube, 205, biological flue gas outlet, 206, biological mixture export, 207, dividing plate, 208, thermal insulation layer, 209, conduction pipe.
Embodiment
For further setting forth the present invention, reach the technique means that predetermined object is taked, below in conjunction with accompanying drawing and preferred embodiment, the technical scheme proposing according to the present invention is elaborated.
A counter combustion-type pyrolysis gasification equipment for biomass waste resources, comprises counter-burning type vapourizing furnace 1 and high-temperature biological mixed gas separator 2.In the body of heater 101 of counter-burning type vapourizing furnace, be provided with feed bin 102, feed bin 102 vertically arranges, and the part of its underpart is as pyrolysis chamber 1022.Between feed bin 102 and the inwall of body of heater 101, be provided with heat exchange chamber 103, heat exchange chamber 103 tops are provided with air-flow buffer chamber 104, and the top of air-flow buffer chamber 104 is provided with the chimney 105 being communicated with high-temperature biological mixed gas separator 2.The biomass waste resource high-temperature gas mixture body that is mixed with biological combustible gas, biological tar, biological acetic acid that high temperature pyrolysis produces in counter-burning type vapourizing furnace enters high-temperature biological mixed gas separator 2 by chimney 105.The top of feed bin 102 is provided with feed bin lid 1021.Between the combustion chamber 106 of pyrolysis chamber 1022 and body of heater 101 bottoms, be provided with fire grate 107, between the bottom of heat exchange chamber 103 and combustion chamber 106, be provided with ignition channel 108, ignition channel 108Jiang pyrolysis chamber 1022 is communicated with the lighting-up tuyere 1081 on body of heater 101 walls, in heat exchange chamber 103, be provided with heat exchanger tube 109, one end of heat exchanger tube 109 is communicated with air-flow buffer chamber 104, the other end is communicated with combustion chamber 106 through igniting path 10 8, is respectively equipped with water-in 1031 and water outlet (1032) on heat exchange chamber 103 sidewalls.
Described high-temperature biological mixed gas separator 2 is provided with housing 201, in housing 201, be provided with Heat Room 202 and standing separation chamber 203, Heat Room 202 is arranged on 203 tops, standing separation chamber, in Heat Room 202, be provided with snakelike or volution or rectilinear heat transfer tube 204, the sidewall of Heat Room 202 is provided with heat exchange water import 2021 and heat exchange water outlet 2022, the top of Heat Room 202 is provided with biological flue gas outlet 205, bottom is provided with biological mixture export 206, the two ends of heat transfer tube 204 are communicated with biological flue gas outlet 205 and biological mixture export 206 respectively, the bottom of heat transfer tube 204 is communicated with the chimney 105 of counter-burning type vapourizing furnace by the high-temperature biological mixed gas import 2011 arranging on housing 201 sidewalls, the biological mixture export 206 of Heat Room 202 is communicated with the biological mixed solution import 2031 at the top of standing separation chamber 203, in standing separation chamber 203, be provided with dividing plate 207, dividing plate 207 is divided into two chambers in left and right by standing separation chamber 203, the bottom of two chambers is communicated with, biological mixed solution import 2031 is positioned at one of them chamber top (Tu Zhongwei left chamber), above the chamber sidewall that is provided with biological mixed solution import 2031, be provided with biological tar light oil outlet 2032, the sidewall top of another chamber is provided with biological acetic acid outlet 2033, in the bottom of standing separation chamber 203, be provided with biological tar heavy oil outlet 2034.
Described water-in 1031 is arranged on to the lower sidewall of heat exchange chamber 103, water outlet 1032 is arranged on the side wall upper part of heat exchange chamber 103.Can remain and in heat exchange chamber 103, be full of heat exchange water, improve heat exchange efficiency, and prevent heat exchanger tube 109 outsides and the inner ingress of air of heat exchange chamber 103 and be corroded.The heat exchange water import 2021 of Heat Room 202 and heat exchange water outlet 2022 can be by same method settings.
Described body of heater 101 bottoms are provided with the ash output hole 1011 being communicated with combustion chamber 106.
Described housing 201 is provided with thermal insulation layer 208.Thermal insulation layer 208 can be arranged on housing 201 inner sides, also can be arranged on outside, or be arranged in the interlayer of housing.Thermal insulation layer 208 can reduce calorific loss, improves the recovery utilization rate of heat.
The biological mixture export 206 of described Heat Room 202 is communicated to the biological mixed solution import 2031 at 203 tops, standing separation chamber by conduction pipe 209, high-temperature biological mixed gas import 2011 is communicated with conduction pipe 209.
Described high-temperature biological mixed gas import 2011 is connected with solid, gas separator, and solid, gas separator can be porcelain filter, Cyclonic separating apparatus or other dust removal installation.
The setting position of described biological tar light oil outlet 2032 is higher than biological acetic acid outlet 2033.
Described housing 201 tops are provided with upper cover 2012, and bottom is provided with lower cover 2013, and biological flue gas outlet 205 and biological tar heavy oil outlet 2034 are separately positioned on upper cover 2012 and lower cover 2013.
Described biological tar light oil outlet 2032, the outlet 2033 of biological acetic acid and biological tar heavy oil outlet 2034 are respectively equipped with valve.
Two chambers in described standing separation chamber 203, can be by open communication reserved between dividing plate 207 and 203 bottoms, standing separation chamber, one or more through holes that also can arrange by dividing plate 207 lower ends are communicated with, or being communicated with communicating pipe by dividing plate 207 lower ends settings.Dividing plate 207 can vertically arrange, also can be obliquely installed, or the form of polylith baffle combination.
Biological flue gas outlet 205 at high-temperature biological mixed gas separator 2 connects aerodynamic force equipment or chimney is set, make the heat transfer tube 204 of high-temperature biological mixed gas separator 2 and the interior generation negative pressure of the heat exchanger tube 109 of counter-burning type vapourizing furnace 1, make the high-temperature gas mixture body producing in Aerodynamic force action current downflow.
When counter combustion-type pyrolysis gasification equipment for biomass waste resources is used: the chimney of counter-burning type vapourizing furnace 105 is connected with high-temperature biological mixed gas separator; The biological flue gas outlet 205 of high-temperature biological mixed gas separator is connected with gas dynamic facility (GDF); Open feed bin lid 1021, feed bin 102 is filled it up with to biomass fuel (raw material), then cover feed bin lid 1021; By water-in 1031, give heat exchange chamber 103 topped up with water; Sealing ash output hole 1011; From lighting-up tuyere 1081, put into pyrophoric fuel and light, containing oxygen air, under Aerodynamic force action, from lighting-up tuyere 1081, entering pyrolysis chamber 1022 and combustion chamber 106 pilot chamber fuels; Then open feed bin lid 1021, enclosed point burner 1081, containing oxygen air, under Aerodynamic force action, from material outlet, enter, by feed bin 102, enter pyrolysis chamber 1022 and combustion chamber 106, indoor section oxidized, release of heat forms high temperature, and indoor remaining fuel, under the condition of high temperature, is carried out pyrolytic gasification reaction and formed high-temperature gas mixture body; High-temperature gas mixture body process heat exchanger tube 109, and implement heat exchange with the water in heat exchange chamber 103, water temperature raises, high-temperature gas cooling; Mixed gas enters high-temperature biological mixed gas separator by the chimney 105 of air-flow buffer chamber 104; The further heat exchange of water in the heat transfer tube 204 that mixed gas enters high-temperature biological mixed gas separator and Heat Room 202, coagulable constituents condensation is laggard enters standing separate chamber 203, obtains biological acetic acid and biological tar after stratification; In mixed gas, isolated biological combustible gas flows out from biological flue gas outlet 205, obtains biological combustible gas.Pyrolysis chamber 1022 and combustion chamber 106 fuels fuel in pyrolysis, combustion processes reduce gradually and form hole, and the fuel in feed bin 102 moves down under self gravitation effect, automatically fills up hole, implement automatic feeding.Biological inflammable gas is for resident's cooking; Biological acetic acid is used for bio-organic fertilizer processed, biology feed additive, Biocidal (bacterium) agent; Biological tar is used for Biocidal processed (bacterium) agent or biogas (bavin) oil, for urban residents' life and production.
Claims (6)
1. a counter combustion-type pyrolysis gasification equipment for biomass waste resources, comprise counter-burning type vapourizing furnace (1) and high-temperature biological mixed gas separator (2), it is characterized in that: in the body of heater of counter-burning type vapourizing furnace (101), be provided with a vertical feed bin (102), between feed bin (102) and the inwall of body of heater (101), be provided with heat exchange chamber (103), heat exchange chamber (103) top is provided with air-flow buffer chamber (104), the top of air-flow buffer chamber (104) is provided with the chimney (105) being communicated with high-temperature biological mixed gas separator (2), the top of feed bin (102) is provided with the feed bin lid (1021) that can open air inlet, the bottom of feed bin (102) is pyrolysis chamber (1022), between the combustion chamber (106) of pyrolysis chamber (1022) and body of heater (101) bottom, be provided with fire grate (107), between the bottom of heat exchange chamber (103) and combustion chamber (106), be provided with ignition channel (108), ignition channel (108) is communicated with pyrolysis chamber (1022) with the lighting-up tuyere (1081) on body of heater (101) wall, in heat exchange chamber (103), be provided with heat exchanger tube (109), one end of heat exchanger tube (109) is communicated with air-flow buffer chamber (104), the other end is communicated with combustion chamber (106) through ignition channel (108), on heat exchange chamber (103) sidewall, be respectively equipped with water-in (1031) and water outlet (1032),
Described high-temperature biological mixed gas separator (2) is provided with housing (201), in housing (201), be provided with Heat Room (202) and standing separation chamber (203), Heat Room (202) is arranged on top, standing separation chamber (203), in Heat Room (202), be provided with snakelike or volution or rectilinear heat transfer tube (204), the sidewall of Heat Room (202) is provided with heat exchange water import (2021) and heat exchange water outlet (2022), the top of Heat Room (202) is provided with biological flue gas outlet (205), bottom is provided with biological mixture export (206), the two ends of heat transfer tube (204) are communicated with biological flue gas outlet (205) and biological mixture export (206) respectively, the bottom of heat transfer tube (204) is communicated with the chimney (105) of counter-burning type vapourizing furnace by the high-temperature biological mixed gas import (2011) arranging on housing (201) sidewall, the biological mixture export (206) of Heat Room (202) is communicated with the biological mixed solution import (2031) at the top of standing separation chamber (203), in standing separation chamber (203), be provided with dividing plate (207), dividing plate (207) is divided into two chambers in left and right by standing separation chamber (203), the bottom of two chambers is communicated with, biological mixed solution import (2031) is positioned at one of them chamber top, in the chamber sidewall top that is provided with biological mixed solution import (2031), be provided with biological tar light oil outlet (2032), the sidewall top of another chamber is provided with biological acetic acid outlet (2033), in the bottom of standing separation chamber (203), be provided with biological tar heavy oil outlet (2034),
The biological mixture export (206) of described Heat Room (202) is communicated to the biological mixed solution import (2031) at top, standing separation chamber (203) by conduction pipe (209), high-temperature biological mixed gas import (2011) is communicated with conduction pipe (209);
The setting position of described biological tar light oil outlet (2032) exports (2033) higher than biological acetic acid.
2. a kind of counter combustion-type pyrolysis gasification equipment for biomass waste resources as claimed in claim 1, it is characterized in that: described water-in (1031) is arranged on the lower sidewall of heat exchange chamber (103), water outlet (1032) is arranged on the side wall upper part of heat exchange chamber (103).
3. a kind of counter combustion-type pyrolysis gasification equipment for biomass waste resources as claimed in claim 1, is characterized in that: described body of heater (101) bottom is provided with the ash output hole (1011) being communicated with combustion chamber (106).
4. a kind of counter combustion-type pyrolysis gasification equipment for biomass waste resources as claimed in claim 1, is characterized in that: described housing (201) is provided with thermal insulation layer (208).
5. a kind of counter combustion-type pyrolysis gasification equipment for biomass waste resources as claimed in claim 1, is characterized in that: described high-temperature biological mixed gas import (2011) is connected with cleaning apparatus.
6. a kind of counter combustion-type pyrolysis gasification equipment for biomass waste resources as claimed in claim 1, it is characterized in that: described housing (201) top is provided with upper cover (2012), bottom is provided with lower cover (2013), and biological flue gas outlet (205) and biological tar heavy oil outlet (2034) are separately positioned on upper cover (2012) and lower cover (2013).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110420412.7A CN102517092B (en) | 2011-12-15 | 2011-12-15 | Counter combustion-type pyrolysis gasification equipment for biomass waste resources |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110420412.7A CN102517092B (en) | 2011-12-15 | 2011-12-15 | Counter combustion-type pyrolysis gasification equipment for biomass waste resources |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102517092A CN102517092A (en) | 2012-06-27 |
| CN102517092B true CN102517092B (en) | 2014-09-24 |
Family
ID=46288168
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110420412.7A Expired - Fee Related CN102517092B (en) | 2011-12-15 | 2011-12-15 | Counter combustion-type pyrolysis gasification equipment for biomass waste resources |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102517092B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109161389B (en) * | 2018-08-16 | 2023-11-03 | 湖北师范大学 | Self-weight spiral progressive biomass efficient energy-saving pyrolysis system |
| TWI704009B (en) * | 2019-10-22 | 2020-09-11 | 行政院原子能委員會核能研究所 | Oil-gas separation system and its use |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1048506A (en) * | 1989-05-02 | 1991-01-16 | 千代田化工建设株式会社 | Processing contains the method and apparatus of the waste gas of dust and chemical pollutant |
| US5562744A (en) * | 1993-06-11 | 1996-10-08 | Enviropower Oy | Method for treating process gas |
| CN2869677Y (en) * | 2005-12-30 | 2007-02-14 | 贾树峰 | Coal gasifying strongy-burning back-burning automatic water-heating boiler |
| CN101638592A (en) * | 2009-05-04 | 2010-02-03 | 李观德 | Method and device for collecting and utilizing waste gas in process of preparing charcoal |
| CN101649226A (en) * | 2009-09-11 | 2010-02-17 | 北京震宇成套电气设备集团 | Method for preparing fuel gas by gasifying biomass materials and device thereof |
| CN101955780A (en) * | 2010-09-17 | 2011-01-26 | 陕西亿鑫生物能源科技开发有限公司 | Co-production system and co-production method for biomass carbon, gas, wood tar and wood vinegar |
-
2011
- 2011-12-15 CN CN201110420412.7A patent/CN102517092B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1048506A (en) * | 1989-05-02 | 1991-01-16 | 千代田化工建设株式会社 | Processing contains the method and apparatus of the waste gas of dust and chemical pollutant |
| US5562744A (en) * | 1993-06-11 | 1996-10-08 | Enviropower Oy | Method for treating process gas |
| CN2869677Y (en) * | 2005-12-30 | 2007-02-14 | 贾树峰 | Coal gasifying strongy-burning back-burning automatic water-heating boiler |
| CN101638592A (en) * | 2009-05-04 | 2010-02-03 | 李观德 | Method and device for collecting and utilizing waste gas in process of preparing charcoal |
| CN101649226A (en) * | 2009-09-11 | 2010-02-17 | 北京震宇成套电气设备集团 | Method for preparing fuel gas by gasifying biomass materials and device thereof |
| CN101955780A (en) * | 2010-09-17 | 2011-01-26 | 陕西亿鑫生物能源科技开发有限公司 | Co-production system and co-production method for biomass carbon, gas, wood tar and wood vinegar |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102517092A (en) | 2012-06-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102604681B (en) | Pyrolytic carbon gasification comprehensive transformation utilization system and method for biomass waste resources | |
| CN102517092B (en) | Counter combustion-type pyrolysis gasification equipment for biomass waste resources | |
| CN102418995B (en) | Multifunctional biomass reverse burning-type hot water boiler | |
| CN102517091B (en) | Counter combustion-type pyrolysis gasification equipment for biomass waste resources | |
| CN102424762B (en) | Counter-burning type biomass waste resource pyrolysis carbon gasification heating equipment | |
| CN102517055B (en) | Multifunctional biomass converter | |
| CN106838992A (en) | Biomass combustion energy-saving and emission-reduction heating system | |
| CN102417837B (en) | Reverse combustion biomass waste resource pyrolysis gasification heating equipment | |
| CN102517095B (en) | Multifunctional separation equipment for high-temperature biological mixed gas | |
| CN1970687A (en) | Circulating fixed bed type bio-mass gasifying equipment | |
| CN102434895B (en) | Multifunctional biomass transformation reversal combustion heating system | |
| CN202346980U (en) | Biomass comprehensive transformation device | |
| CN205443186U (en) | Garbage pyrolytic device | |
| CN202229394U (en) | Energy-saving emission-reducing fire tube boiler with stock bin | |
| CN204689955U (en) | A kind of device of biological material production combustion gas | |
| CN203024184U (en) | Dual-purpose biomass cooking and warming furnace | |
| CN102504844B (en) | Pyrolysis equipment of biomass waste resource pyrolysis carbonization comprehensive conversion system | |
| CN202415488U (en) | Comprehensive biomass conversion device | |
| CN202415489U (en) | Integrated conversion utilization system for pyrolysis and gasification of agricultural waste resources | |
| CN107062597A (en) | A kind of multi-function heating water heater | |
| CN102604682B (en) | Comprehensive waste biomass resource transformation and utilization system and method through pyrolysis and gasification | |
| CN201301303Y (en) | Biomass straw gasification device | |
| CN105042847B (en) | A kind of antirust biomass water heater | |
| CN1936429A (en) | Biological-material-tall stove | |
| CN109268817B (en) | Biomass combustion furnace heating system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140924 Termination date: 20161215 |