CN101191059A - Dynamics gasification furnace and exhaust heat boiler composed by the same - Google Patents

Dynamics gasification furnace and exhaust heat boiler composed by the same Download PDF

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CN101191059A
CN101191059A CNA2006101461960A CN200610146196A CN101191059A CN 101191059 A CN101191059 A CN 101191059A CN A2006101461960 A CNA2006101461960 A CN A2006101461960A CN 200610146196 A CN200610146196 A CN 200610146196A CN 101191059 A CN101191059 A CN 101191059A
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coal
gasification
dynamics
kinetics
heat build
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CN101191059B (en
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周开根
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/133Renewable energy sources, e.g. sunlight

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Abstract

The invention discloses a dynamic gasification furnace and a waste heat boiler formed by the dynamic gasification furnace and relates to gasification equipment using solid fuel to produce synthesis gas. The invention has wide raw material suitability, and the raw materials comprise original msw, biomass, bio-coal briquette, coal-based briquettes, raw coal and loose coal. Through applying the invention, garbage and biomass gasification equipment with low investment, simple operation and easy popularization can be designed, can be operated as conventional boilers and can realize continuous raw material input, continuous deslagging and continuous synthesis gas output. The invention contributes to the active utilization of renewable energy, solves the problem of the treatment of domestic garbage and agricultural and agricultural and forest residues, ensures that the domestic garbage and agricultural and forest residues are transformed into clean energy, on one hand, the problem of environmental protection is solved, on the other hand, the situation of energy crisis is alleviated, creates conditions for promoting the overall coordinated and sustainable development of the economic society, and creates good development chance for rural areas which provide biological resources.

Description

The waste heat boiler of dynamics gasification furnace and formation thereof
Affiliated technical field
The present invention relates to a kind of equipment for gasification, specially refer to the equipment for gasification that a kind of application of solid fuels is produced synthetic gas.
Background technology
Current, be becoming tight global energy day and the sternness day by day of environmental protection situation, concerning China, every year will be from external import a large amount of oil and liquefied gas on the one hand, and be that rubbish, the biomass resource that enriches fails to be utilized effectively on the other hand, major part all is dropped or incinerates, and some place or even rubbish overflow.Along with the development of Chinese national economy and the continuous expansion of city size, rubbish also will rise with 10% ratio, and the content of its objectionable constituent is also more and more higher, as handle badly, will pollute the environment, and have influence on people's life.The most of area of China still adopts landfill method to handle domestic waste at present, this not only need take a large amount of soils, waste resource, and cause secondary pollution easily, the whole nation is stored up farmland area occupied and that damage because of solid waste and has been reached more than 2,000,000 mu; Some area adopts burning method to handle domestic waste, reclaims heat energy and be used for generating or heat supply, but the energy conversion rate of refuse-burning plant is very low, only be 35% less than, have the energy more than 65% to be wasted, even more serious is that the flue gas that burns enters atmosphere and produces secondary pollution.
China's biomass resource is very abundant, there are a large amount of agricultural wastes, fuel wood woods, wood-curing waste available, only the agricultural wastes of stalk, husk and so on just have more than 1,000,000,000 ton every year, amount to more than 500,000,000 ton of standard coal, and other biomass resource still do not have statistics.At present, these biomass resources fail to be utilized effectively, and except that the small portion rural area is used for the fermentation and biogas production, major part is all by directly burning, landfill have fallen.Biomass are directly easily producing coal smoke, flying dust, carbon monoxide and carbon dioxide pollution environment in the combustion processes.
The energy general layout of China is rich coal, few oil, weak breath, the coal resource of use China's abundant can reduce the dependence to oil, but directly fire coal can bring the serious environmental pollution problem, coal is converted into secondary clean energy by gasification meets current China's national situation, but present technology and conversion process to be wasted the closely energy of half.
Day by day exhausted along with the increasingly serious and fossil oil of environment protection situation, human " the increasing income and decreasing expenditure " that must realize the energy, that is: one is to improve the efficient of fuel combustion with the minimizing resource consumption, and realizes that simultaneously clean burning is with the pollution of minimizing to environment; The 2nd, tap a new source of energy, and actively utilize renewable energy source.
Be rubbish, Wood Adhesives from Biomass that clean energy is used how, turn waste into wealth, and alleviate the pressure of petroleum demand with this, until the dependence of breaking away from oil and coal, many scientific research institutions all actively drop into strength and research and develop, this problem is also attracting numerous amateurish inventors' interest, but does not also have the example and the report of commercial applications so far.
The objective of the invention is to manufacture and design a kind of invest rubbish, gasifying biomass equipment low, simple to operate, that be easy to popularize, for actively utilizing the renewable energy source power-assisted.
Summary of the invention
In order to reach above-mentioned goal of the invention, the present invention improves gasification condition by the measure that kinetics heat build-up induced exhaust is set in stove, to reduce power loss, the raising factor of created gase in conversion process.Solid fuel is driven by fire grate to be introduced into that the destructive distillation pyrolysis zone of burner hearth is dried, preheating, pyrolysis and fugitive constituent effusion, anoxycausis, gasification, enters burnt zone again and proceeds combustion gasification, until burning; The synthetic gas of solid fuel gasification enters into kinetics heat build-up induced exhaust, is drawn under the graviational interaction of kinetics heat build-up induced exhaust, wherein gaseous state tar, the C of pyrolysis effusion nH mCarry out cracking or conversion in the kinetics heat build-up induced exhaust, generate the synthetic gas of carbon monoxide and hydrogen.Described kinetics heat build-up induced exhaust is arranged in the insulation fender body of vapourizing furnace, kinetics heat build-up induced exhaust adopts changeable caliber design, when producing heat in the stove, its kinetics function produces suction gravitational effect and compression heat build-up effect, temperature reaches more than 1100 ℃, makes tar, C in the pyrolysis gas nH mEasily cracking or be converted into carbon monoxide and the synthetic gas of hydrogen, and and synthetic gas is drawn; The inlet of kinetics heat build-up induced exhaust is provided with the spin chamber, and the incendiary hot gas flow at first is inhaled into the spin chamber, and the eddy flow guide effect matches with kinetics heat build-up induced exhaust, and its principle of dynamics makes it to produce tornado effect, forces water vapor and gaseous state tar, C nH mThe thorough mixing reaction, the productive rate of increase synthetic gas produces very strong suction power simultaneously, makes the combustion gasification burner hearth form negative pressure naturally, can reduce the input of air and increase the water vapor input, and productive rate and the quality that improves synthetic gas all is beneficial to.The combustion gasification apparatus of vapourizing furnace of the present invention mainly is made up of kinetics heat build-up induced exhaust, destructive distillation pyrolysis zone, burnt zone, fire grate, distribution plenum, damper, steam spray nozzle, wherein: the destructive distillation pyrolysis zone communicates with burnt zone, constitutes the burner hearth of combustion gasification; The top of burnt zone is a kinetics heat build-up induced exhaust, and the inlet of kinetics heat build-up induced exhaust has the spin chamber; Fire grate constitutes the end of combustion gasification burner hearth; Distribution plenum is arranged under the fire grate, steam spray nozzle is arranged in the distribution plenum.Also be provided with the reflection baking in the destructive distillation pyrolysis zone, above the destructive distillation pyrolysis zone, also be provided with simultaneously dechlorination/sweetening agent, rubbish, the fugitive constituent of biomass and pyrolysis gas enter into kinetics heat build-up induced exhaust after removing chlorine component and sulphur component by dechlorination/sweetening agent again, like this, just can not contain hydrogenchloride or other muriate in the synthetic gas of making, just can not generate hypertoxic carcinogens Dioxins during burning, can guarantee that people's is healthy, when adopting the biomass material do not contain rubbish or dechlorination/sweetening agent being admixed when using in the rubbish, above the destructive distillation pyrolysis zone, do not establish dechlorination/sweetening agent; The graviational interaction of the synthetic gas that generates by kinetics heat build-up induced exhaust enters into heat exchange chamber and lowers the temperature; The present invention is sent to water vapor in the combustion gasification burner hearth as vaporized chemical, carries out chemical reaction with red-hot charcoal, generates the synthetic gas based on carbon monoxide, hydrogen; Excessive water vapor enters into kinetics heat build-up induced exhaust, with gaseous state tar, C nH mCarry out oxidation-reduction reaction, generate CO and H 2Hydrogen-rich synthetic gas, the hydrogen-rich synthetic gas of generation enters into heat exchange chamber and lowers the temperature under the graviational interaction of kinetics heat build-up induced exhaust.
Solid fuel of the present invention comprises crude waste, biomass, lower margin coal, raw coal, loose coal wherein one or more or all; Comprise with rubbish or biomass goods through the processing press forming; Comprise with rubbish, the biomass coal of coal as additive; Comprise coal-based moulded coal.
The waste heat boiler that dynamics gasification furnace of the present invention constitutes, it is characterized in that apparatus body mainly is made up of drum (5), heat sink (9), heat exchange chamber (10), kinetics heat build-up induced exhaust (11), destructive distillation pyrolysis zone (25), burnt zone (15), fire grate (23), distribution plenum (19), damper (20), steam spray nozzle (22), feed bin (28), syngas outlet (13), insulation fender body (31), housing (32), wherein: the inlet of kinetics heat build-up induced exhaust (11) is provided with spin chamber (12); Destructive distillation pyrolysis zone (25) and burnt zone (15) constitute the combustion gasification burner hearth; Described kinetics heat build-up induced exhaust is in insulation fender body (31), and kinetics heat build-up induced exhaust (11) wherein, the below of spin chamber (12) are burnt zone (15); Burnt zone (15) directly communicates with destructive distillation pyrolysis zone (25), and reflection baking (26) is arranged at the top of destructive distillation pyrolysis zone (25); Fire grate (23) constitutes the end of combustion gasification burner hearth, and distribution plenum (19) is arranged under the fire grate (23), and steam spray nozzle (22) is arranged in the distribution plenum (19), and air enters into distribution plenum (19) by damper (20); Heat sink (9) be looped around kinetics heat build-up induced exhaust (11) around, heat sink (9), heat sink upper header (8), lower collecting box (37), downtake (34), carbonated drink separator tube (6), drum (5) constitute water circulation system in the stove of waste heat boiler.The present invention adds binding agent, dechlorination/sweetening agent to rubbish and biomass, and the goods that are pressed into to a certain degree with shape use, not only can handled easily, and can improve the gasification efficiency of raw material.Structure of the present invention and operation are all very simple, and mechanized operation and manual operations are all very convenient, can resemble and operate operation the conventional boiler, can realize importing raw material continuously, slag tap, export continuously synthetic gas continuously.
The waste heat boiler of dynamics gasification furnace of the present invention and formation thereof, the used raw material of its combustion gasification is a rubbish, biomass, coal wherein one or more or all, earlier raw material is carried out defibrination, adding the additive mixing again mixes all, compression moulding again/or granulation, send into again and carry out heat build-up reaction gasification in the dynamics gasification furnace, the synthetic gas that generates is by washing, compression, after the cooling, be stored in the gas holder standby, the synthetic gas that is stored in the gas holder is a kind of clean fuel, can be directly used in burning, also can pass through follow-up equipment hydrogen manufacturing, all right synthesizing methanol, liquid fuel of dme and so on or liquefied gas as fuel.The reaction heat that generates in dynamics gasification furnace is reclaimed by waste heat boiler, and institute's producing steam is as vaporized chemical and the generating and the heat supply of vapourizing furnace.
The invention has the beneficial effects as follows: actively utilize renewable energy source, science, reasonably use rubbish, biomass resource, solve the problem of outlet of the wooden matrix waste in domestic refuse, agriculture and forestry organic waste material, wood working tankage, architectural decoration building site, make it to be converted into a kind of energy of cleaning, the one, solve environmental issue, the 2nd, alleviate the energy-intensive situation, create conditions for promoting the economic society All-round, Coordinated and Sustainable Development, and for creating good development opportunity in the rural area that biomass resource is provided.
Description of drawings
The invention provides following accompanying drawing and be further described, but the embodiment of each accompanying drawing and the following stated all is not construed as limiting the invention:
Fig. 1 is a system process skeleton diagram of using the production synthetic gas that dynamics gasification furnace of the present invention constituted.
Fig. 2 is the structure iron of wherein a kind of vapourizing furnace of the present invention.
Fig. 3 is the A-A sectional view of Fig. 2.
Fig. 4 is the structure iron of another kind of vapourizing furnace of the present invention.
Among the figure: 1. relief valve connection, 2. steam valve interface, 3. pressure gauge connection, 4. steam separator, 5. drum, 6. carbonated drink separator tube, 7. inspection/lance door, 8. heat sink upper header, 9. heat sink, 10. heat exchange chamber, 11. kinetics heat build-up induced exhausts, 12. the spin chamber, 13. syngas outlet, 14. temperature sensors, 15. burnt zone, 16. inspection doors, 17. dreg cooling chamber, 18. water seal, 19. distribution plenums, 20. dampers, 21. swirler, 22. steam spray nozzles, 23. fire grates, 24. motion-work wheel, 25. destructive distillation pyrolysis zone, the reflection baking of 26. destructive distillation pyrolysis zone, 27. dechlorination/sweetening agent, 28. feed bins, 29. pyrolysis gas return inlet, 30. the bleed blower fan, 31. insulation fender bodies, 32. housings, 33. explosion trap, 34. downtakes, 35. inspection doors, 36. vapor superheater, 37. lower collecting box, 38. watermarks.
Embodiment
Embodiment shown in Figure 2 is wherein a kind of vapourizing furnace of the present invention, and equipment mainly is made up of drum (5), heat sink (9), heat exchange chamber (10), kinetics heat build-up induced exhaust (11), destructive distillation pyrolysis zone (25), burnt zone (15), fire grate (23), distribution plenum (19), damper (20), steam spray nozzle (22), dreg cooling chamber (17), bleed blower fan (30), feed bin (28), insulation fender body (31), housing (32).Wherein: the inlet of kinetics heat build-up induced exhaust (11) has spin chamber (12) and swirler (21); Destructive distillation pyrolysis zone (25) communicates with burnt zone (15), constitutes the combustion gasification burner hearth; There are dechlorination/sweetening agent (27) and reflection baking (26) in the top of destructive distillation pyrolysis zone (25); The top of burnt zone (15) is swirler (21), spin chamber (12), and the top of spin chamber (12) is a kinetics heat build-up induced exhaust (11); Fire grate (23) constitutes the end of combustion gasification burner hearth; The below of fire grate (23) is distribution plenum (19), and steam spray nozzle (22) is arranged in the distribution plenum (19); Drum (5) and heat sink (9) are made of the interior water circulation system of stove of waste heat boiler heat sink (9), heat sink upper header (8), lower collecting box (37), downtake (34), carbonated drink separator tube (6), drum (5) in heat exchange chamber (10); Heat exchange chamber (10) is made of insulation fender body (31); On insulation fender body (31), explosion trap (33), inspection/lance door (7), inspection door (16) (35) and syngas outlet (13) are arranged.During the equipment operation, rubbish in the feed bin, biomass material are driven the destructive distillation pyrolysis zone (25) that enters into burner hearth by fire grate (23), the thickness of raw material can be regulated by the coal flashboard, raw material is earlier through entering into burnt zone (15) again behind destructive distillation, the pyrolytic gasification, lime-ash after burning unloads falls dreg cooling chamber (17) release waste heat, enter the cinder notch of going into of mucking machine (not shown) again by water seal (18), transport lime-ash by mucking machine.In said process, fugitive constituent that rubbish, biomass carbonization volatilize and pyrolytic vapour are merged into synthetic gas by dechlorination/sweetening agent (27), under the graviational interaction of bleed blower fan (30), return inlet (29) and tangentially enter spin chamber (12) by pyrolysis gas, form whirlwind and enter kinetics heat build-up induced exhaust (11), the tar that contains in the synthetic gas, methane and water vapor are had an effect and cracking and be converted into the synthetic gas of carbon monoxide, hydrogen; Generate the synthetic gas of carbon monoxide, hydrogen at burnt zone (15) water vapor and red-hot carbon generation chemical reaction, the otch by swirler (21) enters spin chamber (12), forms whirlwind and enters kinetics heat build-up induced exhaust (11); This two road synthetic gas is introduced into heat exchange chamber (10) under the graviational interaction of kinetics heat build-up induced exhaust, at heat exchange chamber (10) heat transferred drum (5) and heat sink (9), synthetic gas obtains cooling, synthetic gas volume after the cooling diminishes that severe increases and sedimentation is drawn from outlet (13).Present embodiment is stablized stove interior gasification temperature and stable factor of created gase by damper (20) and steam spray nozzle (22), can realize importing raw material continuously, slag tap, exports continuously synthetic gas continuously.The synthetic gas that equipment is produced is a kind of clean fuel, can be directly used in burning, also can pass through follow-up equipment hydrogen manufacturing, the liquid fuel or the liquefied gas as fuel of all right synthesizing methanol, dme and so on.The raw material that present embodiment uses comprises crude waste, biomass, rubbish, biomass type coal product, raw coal, coal-based moulded coal goods.
Embodiment shown in Figure 4 is an another kind of vapourizing furnace of the present invention, with the difference of last routine embodiment be not have dechlorination/sweetening agent in the top of destructive distillation pyrolysis zone (25), when doing raw material, dechlorination/sweetening agent is added in the raw material with rubbish.
Vapourizing furnace of the present invention is a kind of waste heat boiler, relates to the pressurized vessel of boiler class, when design, manufacturing and use, should be undertaken by the regulation and the rules of national departments concerned.

Claims (10)

1. a dynamics gasification furnace comprises solid-fuelled combustion gasification apparatus, it is characterized in that the combustion gasification apparatus of vapourizing furnace mainly is made up of kinetics heat build-up induced exhaust (11), destructive distillation pyrolysis zone (25), burnt zone (15), fire grate (23); Wherein: destructive distillation pyrolysis zone, burnt zone constitute the burner hearth of combustion gasification.
2. a kind of dynamics gasification furnace according to claim 1 is characterized in that described kinetics heat build-up induced exhaust is arranged in the insulation fender body of vapourizing furnace; Kinetics heat build-up induced exhaust is the design of changeable caliber, produces compression heat build-up effect and self-induced-air effect under thermodynamic activity, makes tar, C in the pyrolysis gas nH mEasily cracking or be converted into carbon monoxide and the synthetic gas of hydrogen in kinetics heat build-up induced exhaust, and in time synthetic gas is drawn.
3. a kind of dynamics gasification furnace according to claim 1 is characterized in that the inlet of kinetics heat build-up induced exhaust also has spin chamber (12); The below of spin chamber is a burnt zone; Burnt zone directly communicates with the destructive distillation pyrolysis zone, and the top of destructive distillation pyrolysis zone also has reflection baking (26).
4. dynamics gasification furnace according to claim 1 is characterized in that the used raw material of combustion gasification is a solid fuel, described solid fuel comprises crude waste, biomass, lower margin coal, raw coal, loose coal wherein one or more or all; Comprise with rubbish or biomass goods through the processing press forming; Comprise with rubbish, the biomass coal of coal as additive; Comprise coal-based moulded coal.
5. a kind of dynamics gasification furnace according to claim 1, it is characterized in that dechlorination/sweetening agent (27) is arranged above the destructive distillation pyrolysis zone, fugitive constituent that solid fuel is overflowed and pyrolysis gas remove behind chlorine component and the sulphur component graviational interaction by kinetics heat build-up induced exhaust by dechlorination/sweetening agent again and enter into heat exchange chamber and lower the temperature.
6. a kind of dynamics gasification furnace according to claim 1 is characterized in that not establishing dechlorination/sweetening agent when not containing rubbish in the solid fuel or dechlorination/sweetening agent being admixed when using in the garbage fuel above the destructive distillation pyrolysis zone.
7. a kind of dynamics gasification furnace according to claim 1, it is characterized in that water vapor is sent to as vaporized chemical the burner hearth of combustion gasification, carry out chemical reaction with red-hot charcoal, generation is based on the synthetic gas of carbon monoxide, hydrogen, and the synthetic gas of generation is incorporated into heat exchange chamber by kinetics heat build-up induced exhaust and lowers the temperature.
8. the waste heat boiler that constitutes of a dynamics gasification furnace is characterized in that apparatus body mainly is made up of drum (5), heat sink (9), heat exchange chamber (10), kinetics heat build-up induced exhaust (11), destructive distillation pyrolysis zone (25), burnt zone (15), fire grate (23), distribution plenum (19), damper (20), steam spray nozzle (22), feed bin (28), syngas outlet (13), insulation fender body (31), housing (32); Wherein: destructive distillation pyrolysis zone (25), burnt zone (15) constitute the burner hearth of combustion gasification.
9. the waste heat boiler that a kind of dynamics gasification furnace according to claim 8 constitutes, it is characterized in that kinetics heat build-up induced exhaust is in insulation fender body (31), the inlet of kinetics heat build-up induced exhaust (11) also has spin chamber (12), and the below of spin chamber (12) is burnt zone (15); Burnt zone (15) directly communicates with destructive distillation pyrolysis zone (25), and reflection baking (26) is arranged at the top of destructive distillation pyrolysis zone (25); Fire grate (23) constitutes the end of combustion gasification burner hearth, and distribution plenum (19) is arranged under the fire grate (23), and steam spray nozzle (22) is arranged in the distribution plenum (19), and air enters into distribution plenum (19) by damper (20); Heat sink (9) be looped around kinetics heat build-up induced exhaust (11) around, heat sink (9), heat sink upper header (8), lower collecting box (37), downtake (34), carbonated drink separator tube (6), drum (5) constitute water circulation system in the stove of waste heat boiler.
10. the waste heat boiler that a kind of dynamics gasification furnace according to claim 8 constitutes, it is characterized in that the used raw material of combustion gasification be rubbish, biomass, coal wherein one or more or all, earlier raw material is carried out defibrination, adding the additive mixing again mixes all, compression moulding again/or granulation, send into again and carry out heat build-up reaction gasification in the dynamics gasification furnace.
CN2006101461960A 2006-11-22 2006-11-22 Dynamics gasification furnace and exhaust heat boiler composed by the same Expired - Fee Related CN101191059B (en)

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101451707A (en) * 2008-10-06 2009-06-10 冼泰来 Process flow for zero discharge rubbish power generation comprehensive utilization plant
CN102002375A (en) * 2010-12-16 2011-04-06 程培胜 New method for preparing industrial gas or civil gas by cracking garbage and biomass serving as raw materials at high temperature
CN101629715B (en) * 2008-07-17 2011-09-07 周德国 Horizontal type biomass energy furnace
CN101565635B (en) * 2009-06-08 2013-03-20 南京林业大学 Grate-type gasifier for gasifying agriculture and forestry biomass materials
CN103484164A (en) * 2013-09-13 2014-01-01 广州迪森热能技术股份有限公司 Biomass waste heat steam gasification heating system
CN103759415A (en) * 2014-02-25 2014-04-30 赵永万 Energy-saving environment-friendly type back burning boiler
CN105157216A (en) * 2015-08-31 2015-12-16 太仓英达锅炉设备有限公司 Novel boiler device
CN105588127A (en) * 2015-12-29 2016-05-18 广州市祈雅典锅炉有限公司 Boiler combustion system adopting biomass gasification device
CN106698340A (en) * 2016-12-08 2017-05-24 北京神雾环境能源科技集团股份有限公司 Hydrogen production system and method utilizing garbage
CN106895431A (en) * 2016-01-28 2017-06-27 孟氏锅炉(北京)有限公司 A kind of water-gas is produced and burns Integrated Combustion method and its combustion apparatus
CN110028989A (en) * 2019-04-19 2019-07-19 哥尔环保科技(杭州)有限公司 A kind of the reduction process equipment and its operating procedure of water-gas
CN112625753A (en) * 2020-12-18 2021-04-09 安徽香杨新能源科技发展股份有限公司 Cooling device for biomass gas production

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101629715B (en) * 2008-07-17 2011-09-07 周德国 Horizontal type biomass energy furnace
CN101451707A (en) * 2008-10-06 2009-06-10 冼泰来 Process flow for zero discharge rubbish power generation comprehensive utilization plant
CN101565635B (en) * 2009-06-08 2013-03-20 南京林业大学 Grate-type gasifier for gasifying agriculture and forestry biomass materials
CN102002375A (en) * 2010-12-16 2011-04-06 程培胜 New method for preparing industrial gas or civil gas by cracking garbage and biomass serving as raw materials at high temperature
CN103484164A (en) * 2013-09-13 2014-01-01 广州迪森热能技术股份有限公司 Biomass waste heat steam gasification heating system
CN103759415A (en) * 2014-02-25 2014-04-30 赵永万 Energy-saving environment-friendly type back burning boiler
CN105157216A (en) * 2015-08-31 2015-12-16 太仓英达锅炉设备有限公司 Novel boiler device
CN105588127A (en) * 2015-12-29 2016-05-18 广州市祈雅典锅炉有限公司 Boiler combustion system adopting biomass gasification device
CN105588127B (en) * 2015-12-29 2019-04-26 广州市祈雅典环保科技有限公司 Using the boiler combustion system of biomass gasification device
CN106895431A (en) * 2016-01-28 2017-06-27 孟氏锅炉(北京)有限公司 A kind of water-gas is produced and burns Integrated Combustion method and its combustion apparatus
CN106698340A (en) * 2016-12-08 2017-05-24 北京神雾环境能源科技集团股份有限公司 Hydrogen production system and method utilizing garbage
CN110028989A (en) * 2019-04-19 2019-07-19 哥尔环保科技(杭州)有限公司 A kind of the reduction process equipment and its operating procedure of water-gas
CN110028989B (en) * 2019-04-19 2021-06-15 哥尔环保科技(杭州)有限公司 Water gas reduction processing equipment and operation process thereof
CN112625753A (en) * 2020-12-18 2021-04-09 安徽香杨新能源科技发展股份有限公司 Cooling device for biomass gas production
CN112625753B (en) * 2020-12-18 2021-08-24 安徽香杨新能源科技发展股份有限公司 Cooling device for biomass gas production

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