CN201003046Y - Dynamic gasification oven for producing synthesized gas using garbage, biomass as material - Google Patents
Dynamic gasification oven for producing synthesized gas using garbage, biomass as material Download PDFInfo
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- CN201003046Y CN201003046Y CNU200620159284XU CN200620159284U CN201003046Y CN 201003046 Y CN201003046 Y CN 201003046Y CN U200620159284X U CNU200620159284X U CN U200620159284XU CN 200620159284 U CN200620159284 U CN 200620159284U CN 201003046 Y CN201003046 Y CN 201003046Y
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- biomass
- rubbish
- raw material
- synthetic gas
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- 239000002028 Biomass Substances 0.000 title claims abstract description 41
- 238000002309 gasification Methods 0.000 title claims abstract description 22
- 239000010813 municipal solid waste Substances 0.000 title claims description 32
- 239000000463 material Substances 0.000 title claims description 7
- 239000003245 coal Substances 0.000 claims abstract description 19
- 239000002994 raw material Substances 0.000 claims abstract description 17
- 239000002699 waste material Substances 0.000 claims abstract description 12
- 238000000197 pyrolysis Methods 0.000 claims description 51
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 42
- 238000006298 dechlorination reaction Methods 0.000 claims description 13
- 235000003599 food sweetener Nutrition 0.000 claims description 13
- 238000004519 manufacturing process Methods 0.000 claims description 13
- 239000003765 sweetening agent Substances 0.000 claims description 13
- 238000009826 distribution Methods 0.000 claims description 8
- 238000009413 insulation Methods 0.000 claims description 8
- 238000002485 combustion reaction Methods 0.000 claims description 5
- 238000009825 accumulation Methods 0.000 claims description 4
- 238000013461 design Methods 0.000 claims description 4
- 238000011068 loading method Methods 0.000 claims description 4
- 239000000654 additive Substances 0.000 claims description 2
- 230000000996 additive effect Effects 0.000 claims description 2
- 238000012545 processing Methods 0.000 claims description 2
- 238000011161 development Methods 0.000 abstract description 4
- 239000010791 domestic waste Substances 0.000 abstract description 4
- 230000001737 promoting effect Effects 0.000 abstract description 2
- 230000015572 biosynthetic process Effects 0.000 abstract 2
- 238000003786 synthesis reaction Methods 0.000 abstract 2
- 238000000151 deposition Methods 0.000 abstract 1
- 230000002349 favourable effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 25
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- 239000001257 hydrogen Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000007921 spray Substances 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 5
- 229910002091 carbon monoxide Inorganic materials 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000007689 inspection Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 230000003993 interaction Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000002154 agricultural waste Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 229960004424 carbon dioxide Drugs 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Images
Classifications
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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
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a dynamics gasification furnace which produces synthesis gas by utilizing waste and biomass as raw material, and relates to a gasification device which can produce synthesis gas by utilizing biomass. The suitability of raw material of the utility model is wide, comprising waste and biomass, biomass type coal, basic type coal, raw coal and scattering coal. A low investment, easy operation and easy popularization waste and biomass gasification device is formed by utilizing the utility model, which contributes to the active renewable energy sources utilization. The utility model solves the depositing problem of the household waste and agriculture and forest waste, and translates the household waste and agriculture and forest waste into clean energy, which firstly solves the problem of environment protection and secondly eases the situation of energy supply pressure, thereby creating condition for promoting all-round, harmonious and sustainable development of the economy and society and creating favorable opportunities for developing country which provides biomass resource.
Description
Affiliated technical field
The utility model relates to a kind of equipment for gasification, specially refers to the equipment for gasification that a kind of applying biological mass-energy 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.
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 utility model content
The purpose of this utility model 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.
In order to reach above-mentioned utility model purpose, the utility model improves gasification condition by the measure that kinetics heat build-up induced exhaust, destructive distillation pyrolysis zone, burnt zone, the pre-split plot of tar/methane are set in stove.Described kinetics heat build-up induced exhaust is arranged in the insulation fender body of vapourizing furnace, and kinetics heat build-up induced exhaust adopts the design of changeable caliber, produces compression heat build-up effect and self-induced-air effect under thermodynamic activity, makes tar, methane, 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, improve vaporization rate, also make destructive distillation pyrolysis zone, burnt zone, the pre-split plot of tar/methane not have just to form negative pressure under the induced draft fan effect, when operation, can reduce the input of air and increase the water vapor input, productive rate and the quality that improves synthetic gas all is beneficial to.The combustion gasification apparatus of vapourizing furnace of the present utility model mainly is made up of destructive distillation pyrolysis zone, burnt zone, the pre-split plot of tar/methane, kinetics heat build-up induced exhaust, fire grate, distribution plenum, damper, steam spray nozzle, wherein: the destructive distillation pyrolysis zone communicates with burnt zone, the top of burnt zone is the pre-split plot of tar/methane, and the top of the pre-split plot of tar/methane is a kinetics heat build-up induced exhaust; Steam spray nozzle is installed in distribution plenum; Also be provided with the reflection baking in the destructive distillation pyrolysis zone, the top of the pyrolysis zone of destructive distillation simultaneously also is provided with dechlorination/sweetening agent, rubbish, the fugitive constituent of biomass and pyrolysis gas enter into the pre-split plot of tar/methane after removing chlorine component and sulphur component by dechlorination/sweetening agent again, 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; Also be provided with accumulation of heat reflection top at burnt zone; The utility model is sent to water vapor in destructive distillation pyrolysis zone, burnt zone, the pre-split plot of tar/methane, the kinetics heat build-up induced exhaust as vaporized chemical, carries out chemical reaction with red-hot charcoal, generates the synthetic gas based on-carbonoxide, hydrogen; In kinetics heat build-up induced exhaust, temperature will reach about 1100 ℃, water vapor and tar, methane, 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 by kinetics heat build-up induced exhaust and lowers the temperature.
Vapourizing furnace body of the present utility model mainly is made up of drum (1), heat pipe (3), heat exchange chamber (24), destructive distillation pyrolysis zone (19), burnt zone (14), the pre-split plot of tar/methane (5), kinetics heat build-up induced exhaust (4), fire grate (18), distribution plenum (12), damper (13), loading hopper (22), syngas outlet (6), insulation fender body (25), structure and operation are all very simple, mechanized operation and manual operations are all very convenient, can resemble to operate operation the conventional boiler.
Rubbish described in the utility model, biomass material comprise wherein a kind of of crude waste, biomass or two kinds; Comprise with rubbish or biomass goods through the processing press forming; Comprise with rubbish, the biomass coal of coal as additive; Comprise with the coal being the moulded coal of main component; Comprise raw coal or diffusing coal.Rubbish and biomass are added binding agent, dechlorination/sweetening agent, 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, the utility model preferably adopts this mode.
The beneficial effects of the utility model are: 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 utility model provides following accompanying drawing to be further described, but the embodiment of each accompanying drawing and the following stated does not all constitute restriction of the present utility model:
Fig. 1 is the structure iron of wherein a kind of vapourizing furnace of the present utility model.
Fig. 2 is the structure iron of another kind of vapourizing furnace of the present utility model.
Among the figure: 1. drum, 2. inspection/lance door, 3. heat pipe, 4. kinetics heat build-up induced exhaust, the 5. pre-split plot of tar/methane, 6. syngas outlet, 7. temperature sensor 8. dries by the fire behind the burnt zone, 9. inspection door, 10. dreg cooling chamber, 11. water seals, 12. distribution plenums, 13. damper, 14. burnt zones, 15. burnt zone accumulation of heats reflection top, 16. the reflection of destructive distillation pyrolysis zone baking, 17. steam spray nozzles, 18. fire grates, 19. the destructive distillation pyrolysis zone, 20. pyrolysis gas return inlet, 21. dechlorinations/sweetening agent, 22. loading hopper, 23. bleed blower fans, 24. heat exchange chambers, 25. insulation fender body, 26. explosion trap, 27. vapor superheaters, 28. housings.
Embodiment
Embodiment shown in Figure 1 is wherein a kind of vapourizing furnace of the present utility model, and equipment mainly is made up of drum (1), heat pipe (3), heat exchange chamber (24), destructive distillation pyrolysis zone (19), burnt zone (14), the pre-split plot of tar/methane (5), kinetics heat build-up induced exhaust (4), fire grate (18), distribution plenum (12), damper (13), steam spray nozzle (17), dreg cooling chamber (10), bleed blower fan (23), loading hopper (22), insulation fender body (25).Wherein: destructive distillation pyrolysis zone (19) communicates with burnt zone (14), and there is dechlorination/sweetening agent (21) top of destructive distillation pyrolysis zone (19), also has reflection baking (16); Burnt zone (14) also has accumulation of heat reflection top (15); The top of burnt zone (14) is the pre-split plot of tar/methane (5), and the top of the pre-split plot of tar/methane (5) is a kinetics heat build-up induced exhaust (4); Fire grate (18) is applied between destructive distillation pyrolysis zone (19) and the burnt zone (14); The below of fire grate (18) is distribution plenum (12), and steam spray nozzle (17) is arranged in the distribution plenum (12); Drum (1) and heat pipe (3) are in heat exchange chamber (24); Heat exchange chamber (24) is made of insulation fender body (25); On insulation fender body (25), explosion trap (26), inspection/lance door (2), inspection door (9) and syngas outlet (6) are arranged.During the equipment operation, rubbish in the hopper, biomass material are driven by fire grate (18) and enter destructive distillation pyrolysis zone (19), the thickness of raw material can be regulated by the coal flashboard, raw material is earlier through entering into burnt zone (14) again behind destructive distillation, the pyrolytic gasification, lime-ash after burning unloads falls dreg cooling chamber's release waste heat, enter the cinder notch of going into of mucking machine again by water seal (11), transport lime-ash by mucking machine.In said process, rubbish, fugitive constituent that biomass carbonization volatilizes and pyrolytic vapour are merged into synthetic gas by dechlorination/sweetening agent (21), under the graviational interaction of bleed blower fan (23), return inlet (20) and enter the pre-split plot of tar/methane (5) by pyrolysis gas, kinetics heat build-up induced exhaust (4), the tar that contains in the synthetic gas, methane and water vapor are had an effect and cracking and be converted into carbon monoxide, the synthetic gas of hydrogen, in burnt zone (14), water vapor and red-hot carbon generation chemical reaction and generate carbon monoxide, the synthetic gas of hydrogen, this two road synthetic gas is drawn into heat exchange chamber (24) under the graviational interaction of kinetics heat build-up induced exhaust (4), at heat exchange chamber (24) heat transferred drum (1) and heat pipe (3), synthetic gas obtains cooling, synthetic gas volume after the cooling diminishes that severe increases and sedimentation is drawn from outlet (6).Present embodiment is stablized factor of created gase and the interior gasification temperature of stable stove by damper (13) and steam spray nozzle (17), can realize exporting continuously synthetic gas.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 product.
Embodiment shown in Figure 2 is an another kind of vapourizing furnace of the present utility model, with the difference of last routine embodiment be not have dechlorination/sweetening agent in the top of destructive distillation pyrolysis zone (19), when doing raw material, dechlorination/sweetening agent is added in the raw material with rubbish.
Vapourizing furnace of the present utility model 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 (8)
1. be the dynamics gasification furnace of raw material production synthetic gas with rubbish, biomass, comprise the combustion gasification cell structure, the combustion gasification apparatus that it is characterized in that vapourizing furnace mainly is made up of kinetics heat build-up induced exhaust, destructive distillation pyrolysis zone, burnt zone, the pre-split plot of tar/methane, and wherein: kinetics heat build-up induced exhaust is arranged in the insulation fender body of vapourizing furnace; Kinetics heat build-up induced exhaust is above the pre-split plot of tar/methane; The below of the pre-split plot of tar/methane is a burnt zone; Burnt zone communicates with the destructive distillation pyrolysis zone.
2. according to claim 1 is the dynamics gasification furnace of raw material production synthetic gas with rubbish, biomass, it is characterized in that described kinetics heat build-up induced exhaust is changeable caliber design.
3. according to claim 1 is the dynamics gasification furnace of raw material production synthetic gas with rubbish, biomass, it is characterized in that there is dechlorination/sweetening agent the top of destructive distillation pyrolysis zone.
4. according to claim 1 is the dynamics gasification furnace of raw material production synthetic gas with rubbish, biomass, it is characterized in that above the destructive distillation pyrolysis zone, not establishing dechlorination/sweetening agent when adopting the biomass material do not contain rubbish or dechlorination/sweetening agent being admixed when using in the rubbish.
5. according to claim 1 is the dynamics gasification furnace of raw material production synthetic gas with rubbish, biomass, it is characterized in that the destructive distillation pyrolysis zone also has the reflection baking.
6. according to claim 1 is the dynamics gasification furnace of raw material production synthetic gas with rubbish, biomass, it is characterized in that burnt zone also has accumulation of heat reflection top.
7. be the dynamics gasification furnace of raw material production synthetic gas with rubbish, biomass, it is characterized in that the vapourizing furnace body mainly is made up of drum (1), heat pipe (3), heat exchange chamber (24), destructive distillation pyrolysis zone (19), burnt zone (14), the pre-split plot of tar/methane (5), kinetics heat build-up induced exhaust (4), fire grate (18), distribution plenum (12), damper (13), loading hopper (22), syngas outlet (6), insulation fender body (25).
According to claim 1 or 7 described be the dynamics gasification furnace of raw material production synthetic gas with rubbish, biomass, it is characterized in that described rubbish, biomass material comprise wherein a kind of of crude waste, biomass or two kinds; Comprise with rubbish or biomass goods through the processing press forming; Comprise with rubbish, the biomass coal of coal as additive.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200620159284XU CN201003046Y (en) | 2006-11-19 | 2006-11-19 | Dynamic gasification oven for producing synthesized gas using garbage, biomass as material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200620159284XU CN201003046Y (en) | 2006-11-19 | 2006-11-19 | Dynamic gasification oven for producing synthesized gas using garbage, biomass as material |
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| Publication Number | Publication Date |
|---|---|
| CN201003046Y true CN201003046Y (en) | 2008-01-09 |
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| CNU200620159284XU Expired - Fee Related CN201003046Y (en) | 2006-11-19 | 2006-11-19 | Dynamic gasification oven for producing synthesized gas using garbage, biomass as material |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101818891A (en) * | 2010-04-20 | 2010-09-01 | 浙江金锅锅炉有限公司 | Industrial boiler for burning bio-briquettes |
| CN101560408B (en) * | 2008-09-03 | 2012-09-19 | 周开根 | Gasification system of garbage and organic waste and device thereof |
| CN106678822A (en) * | 2017-01-23 | 2017-05-17 | 广西威荣环保科技有限公司 | Household refuse direct heating oxygen-deficient gasification kiln |
| CN108286703A (en) * | 2017-12-29 | 2018-07-17 | 汪逸凡 | A kind of anti-grease biomass boiler |
-
2006
- 2006-11-19 CN CNU200620159284XU patent/CN201003046Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101560408B (en) * | 2008-09-03 | 2012-09-19 | 周开根 | Gasification system of garbage and organic waste and device thereof |
| CN101818891A (en) * | 2010-04-20 | 2010-09-01 | 浙江金锅锅炉有限公司 | Industrial boiler for burning bio-briquettes |
| CN101818891B (en) * | 2010-04-20 | 2011-08-31 | 浙江金锅锅炉有限公司 | Industrial boiler for burning bio-briquettes |
| CN106678822A (en) * | 2017-01-23 | 2017-05-17 | 广西威荣环保科技有限公司 | Household refuse direct heating oxygen-deficient gasification kiln |
| CN108286703A (en) * | 2017-12-29 | 2018-07-17 | 汪逸凡 | A kind of anti-grease biomass boiler |
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