CN201031219Y - Multifunctional integrated circulation clean-up combustion pot - Google Patents
Multifunctional integrated circulation clean-up combustion pot Download PDFInfo
- Publication number
- CN201031219Y CN201031219Y CNU2006200226155U CN200620022615U CN201031219Y CN 201031219 Y CN201031219 Y CN 201031219Y CN U2006200226155 U CNU2006200226155 U CN U2006200226155U CN 200620022615 U CN200620022615 U CN 200620022615U CN 201031219 Y CN201031219 Y CN 201031219Y
- Authority
- CN
- China
- Prior art keywords
- pipe
- heater
- pyrolysis device
- storehouse
- flue
- 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
- 238000002485 combustion reaction Methods 0.000 title abstract description 5
- 238000000197 pyrolysis Methods 0.000 claims abstract description 15
- 239000003245 coal Substances 0.000 claims abstract description 13
- 230000007306 turnover Effects 0.000 claims abstract description 5
- 239000006200 vaporizer Substances 0.000 claims description 9
- 239000003054 catalyst Substances 0.000 claims description 2
- 238000002309 gasification Methods 0.000 abstract description 8
- 239000002699 waste material Substances 0.000 abstract description 4
- 239000010902 straw Substances 0.000 abstract description 3
- 239000002023 wood Substances 0.000 abstract description 3
- 230000003197 catalytic effect Effects 0.000 abstract 3
- 241000209504 Poaceae Species 0.000 abstract 1
- 241000209140 Triticum Species 0.000 abstract 1
- 235000021307 Triticum Nutrition 0.000 abstract 1
- -1 firewood Substances 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000000428 dust Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 4
- 239000002956 ash Substances 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- 239000003034 coal gas Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 244000025254 Cannabis sativa Species 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011499 joint compound Substances 0.000 description 1
- 239000003077 lignite Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Images
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Solid-Fuel Combustion (AREA)
Abstract
The utility model relates to an integrally multifunctional circulating purification gas generator, and is characterized in that a once-through flue is arranged in a furnace body, the upper portion of the flue is provided with a loading hopper for the coal to enter, the lower portion is provided with a furnace bar disc, a waste cabin is arranged between the lower portion of the furnace bar disc and a furnace body base, a primary pyrolysis device and a secondary pyrolysis device are both mounted outside the furnace body, a rotatable panel turnover is arranged between the loading hopper and the internal portion of the furnace body, a helical cyclone duct is arranged in the waste cabin, one end of the cyclone duct is connected with an air inlet pipe, the other end is connected till the position which is below the furnace bar disc, an annular catalytic cabin is arranged in the flue which is arranged above the furnace bar disc, two ports of the catalytic cabin are respectively communicated with the primary pyrolysis device and the secondary pyrolysis device which are both arranged outside the furnace body, and a gasification chamber is arranged above the catalytic cabin. The gas generator can use any coals, which breaks through the limitation of regions, and the utility model can be used in all the places of the country and is provided with small pollution, full combustion, and saving energy source. The utility model relates to an environment-friendly type product, needs no people to watch for, and is applicable to all the coals, grasses, wood, firewood, straws, and wheat straws.
Description
Technical field:
The utility model relates to a kind of coal-fired gasification producer, particularly a kind of multifunction integrated circulation purifying gas generator with many fuel, environment-friendly type.
Background technology:
At present, the existing vapourizing furnace of economizing on coal, though coal gas and hot water can be provided, but its coal-fired kind is single, the waste gas that blower fan when work smoke exhaust pipe also will have a dust directly enters and causes serious environmental to pollute in the air, and coal gas is collected also incomplete, exists not environmental protection, coal single, and tar has caused severe contamination to body of heater and environment, is subjected to shortcomings such as territorial restrictions.Therefore, be necessary prior art is innovated at above deficiency.
Summary of the invention:
The purpose of this utility model is to provide a kind of multifunction integrated circulation purifying gas generator, and its structure forms with reference to the relevant theory innovation exploitation with gas gasification stove and treating plant structure of boiler design on traditional producer gas generator principle basis.It is a raw material with the resistates of grass, wood, bavin standing grain, stalk, production of forestry or waste material and brown coal, mud coal etc., at a certain temperature, organic matter in the raw material and charcoal and tar and vaporized chemical generation chemical reaction generate the inflammable gas that contains carbon monoxide, hydrogen, methane gas etc.
The purpose of this utility model reaches by following technical measures: multifunction integrated circulation purifying gas generator, the through type flue is arranged in the body of heater, the into loading hopper of coal is arranged at flue top, stove rod plate is arranged at the bottom, between stove rod plate bottom and the base of furnace body reject bin is arranged, cracker and second pyrolysis device are equipped with in the body of heater outside, and a rotating turnover panel is arranged between loading hopper and the body of heater inside; Be furnished with spirrillum whirlwind road in the reject bin, whirlwind road one end connects inlet pipe, and the other end is connected to below the stove rod plate; Be provided with the ring catalyst storehouse in the flue above the stove rod plate, the two-port in catalyzer storehouse is communicated with cracker that is arranged in the body of heater outside and second pyrolysis device respectively, and the top of catalyzer storehouse is vaporizer.
Connecting pipe was communicated with the entrance end in intravital vaporizer of stove and catalyzer storehouse respectively about a described cracker passed through, and an extra heavy pipe road is arranged between the connecting pipe up and down, was connected with a water-sealed valve on the extra heavy pipe road; The open and close valve assembly is equipped with at top, extra heavy pipe road, and the burnt pipe of collection is arranged at the bottom, and the burnt pipe of collection returns the tar pipe by one and is connected with inlet pipe.
Described second pyrolysis device is fixed in outside the body of heater, and the bottom is communicated with the exit end in catalyzer storehouse, and top is connected to the gas outlet pipe that communicates with user pipe.
The utility model compared with prior art has following advantage: the gas that once can prevent nuisances such as a large amount of carbonateds, sulfurous gas, dust with the second pyrolysis fly-ash separator in the body of heater both sides enters air, causes air contaminated; The inlet pipe that the water vapour of novelty exports the bottom reject bin to becomes vaporized chemical can improve coal gasification efficient, improves output gas quality, burning better with the air mixed that gas blower is blown into; This coal-fired gasification producer can use any coal, has broken through geographic limitation, can both conveniently use in all places, the whole nation, benefits popularization, and this coal-fired gasification producer pollutes little, and the energy is saved in burning fully, is a kind of environmentally friendly machine.
The utility model does not need personnel to wait for, and is applicable to all coals and grass, wood, bavin standing grain, stalk, straw.
Description of drawings:
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is the rear view of Fig. 1.
Fig. 3 is the cross-sectional view of body of heater.
Embodiment: in conjunction with the accompanying drawings the utility model is described further.
As shown in the figure, the utility model mainly comprises the gas producer body, parts such as combustion gas cracker, and the into loading hopper 2 of coal is arranged at body of heater 1 top, design has a rotating turnover panel between loading hopper and the body of heater inside, rotates turnover panel operating stick 3 and the coal charge in the loading hopper can be shaken off in body of heater.
Connecting pipe is communicated with intravital vaporizer of stove and catalyzer storehouse respectively to adopt the dust separating cracker 5 of water-seal principle to pass through up and down, be connected with an extra heavy pipe road 6 up and down between the pipeline, one water-sealed valve 19 is installed on the extra heavy pipe road, water-sealed valve is one and is trapezoidal or flaring valve bonnet structure that its surface arrangement that feeds in the water surface has several eyelets.Open and close valve assembly 4 is equipped with at top, extra heavy pipe road, can outwards discharge high-temperature vapor, and the burnt pipe 8 of collection is arranged at bottom, extra heavy pipe road, and the burnt pipe of collection returns tar pipe 9 by one and is connected with inlet pipe 12.
Be designed to the through type flue in the body of heater, stove rod plate 22 is arranged at the flue bottom, and reject bin 10 is arranged between stove rod plate bottom and the base of furnace body, and whirlwind road 23 is arranged in the reject bin, has on its sidewall to lead to the outer ash output hole 11 of body of heater, opens sealed ash output hole and can remove lime-ash.Connect inlet pipe along spirrillum whirlwind road one end that the reject bin inwall is arranged, inlet pipe links to each other with body of heater gas blower outward again.The other end in whirlwind road is connected to below the stove rod plate.Stove rod plate top is catalyzer storehouse 20, is provided with refractory brick blocks 21 between the catalyzer storehouse in stove rod plate and stove, plays the effect that i.e. cooling provides waste heat again.Have a plurality of catalyzer mouths 7 that communicate with the catalyzer storehouse on the furnace body outer wall, catalyzer joins in the catalyzer storehouse by the catalyzer mouth, is vaporizer above the catalyzer storehouse.At the body of heater middle part sealed sight burner 13 is arranged, also can light a fire and remove the gred by this mouthful.
Be communicated with a steam output tube 14 between second pyrolysis device 16 and the inlet pipe 12 that tangentially is installed on the reject bin, water vapour becomes vaporized chemical to be transported to vaporizer in inlet pipe to help combustion-supportingly, increase coal gasification efficient, improve the output gas quality with air mixed that gas blower is blown into.
Working process of the present utility model: raw material is added by loading hopper, and gas blower will be blown into the intravital vaporizer of stove as the air of vaporized chemical to be mixed with raw material to burn and promptly produce elementary gas.Elementary gas enters a cracker by the pipeline of upper of furnace body to carry out the first time and filters, reduced particulate matter and dust impurity wherein through this time filtration, can effectively reduce carbonic acid gas and black smoke concentration, become the pure inflammable gas that is cleaned after elementary gas filtration and the cooling, be back to by the pipeline of a cracker bottom and carry out catalyzed reaction in the catalyzer storehouse, its combustion value of the liquid cracked oil of generation is in 3.9-4.1 ten thousand kilojoules.One ton of coal approximately can produce 300 kilograms of cracked oils, output value height, and security is good.The utility model adopts low temperature pyrolyzer, and the cracking working temperature utilizes the waste heat in the burner hearth to meet the demands about 350 degree, and therefore the oxynitride that generates is very low, and environment is not almost polluted.High burning-value inflammable gas after catalyzed reaction enters to be mixed by water cooler and filtering and in the second pyrolysis device that clear device forms coal gas is filtered once more and cool off, and is delivered to user pipe by gas outlet pipe 18 after treatment.The elementary gas-cooled while, separated tar, dust fall into the burnt pipe of the collection that is connected thick tracheae bottom, and the burnt pipe of collection returns tar pipe coupling inlet pipe by one, and useless tar is blown into vaporizer along with the air of inlet pipe and raw material burns.This installs integrated equipment, decomposes tar by cracking, and waste oil is utilized effectively.Become the inflammable gas of high burning-value after the inflammable gas process catalyzer storehouse generation catalyzed reaction, combustion value than traditional combustion exceeds one times, for example, the fuel value of common fire coal reaches more than the 2000-3000 kilocalorie through the fuel value of the high burning-value inflammable gas after the pyrolysis gasification about 1000 kilocalories.
Claims (5)
1. multifunction integrated circulation purifying gas generator, the through type flue is arranged in the body of heater, the into loading hopper of coal is arranged at flue top, stove rod plate is arranged at the bottom, between stove rod plate bottom and the base of furnace body reject bin is arranged, cracker and second pyrolysis device are equipped with in the body of heater outside, it is characterized in that: be furnished with spirrillum whirlwind road in the reject bin, whirlwind road one end connects inlet pipe, and the other end is connected to below the stove rod plate; Be provided with the ring catalyst storehouse in the flue above the stove rod plate, the two-port in catalyzer storehouse is communicated with cracker that is arranged in the body of heater outside and second pyrolysis device respectively, and the top of catalyzer storehouse is vaporizer.
2. multifunction integrated circulation purifying gas generator according to claim 1 is characterized in that: a rotating turnover panel is arranged between the loading hopper of body of heater and the body of heater inside.
3. multifunction integrated circulation purifying gas generator according to claim 1, it is characterized in that: connecting pipe was communicated with the entrance end in intravital vaporizer of stove and catalyzer storehouse respectively about one time cracker passed through, one extra heavy pipe road is arranged between the connecting pipe up and down, be connected with a water-sealed valve on the extra heavy pipe road.
4. according to claim 1 or 3 described multifunction integrated circulation purifying gas generators, it is characterized in that: the open and close valve assembly is equipped with at top, extra heavy pipe road, and the burnt pipe of collection is arranged at the bottom, and the burnt pipe of collection returns the tar pipe by one and is connected with inlet pipe.
5. multifunction integrated circulation purifying gas generator according to claim 1 is characterized in that: the second pyrolysis device is fixed in outside the body of heater, and the bottom is communicated with the exit end in catalyzer storehouse, and top is connected to the gas outlet pipe that communicates with user pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200226155U CN201031219Y (en) | 2006-12-18 | 2006-12-18 | Multifunctional integrated circulation clean-up combustion pot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200226155U CN201031219Y (en) | 2006-12-18 | 2006-12-18 | Multifunctional integrated circulation clean-up combustion pot |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201031219Y true CN201031219Y (en) | 2008-03-05 |
Family
ID=39163113
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2006200226155U Expired - Fee Related CN201031219Y (en) | 2006-12-18 | 2006-12-18 | Multifunctional integrated circulation clean-up combustion pot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201031219Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105295969A (en) * | 2014-07-24 | 2016-02-03 | 北京南亚节能技术研究院 | Straw bio-energy preparation method |
| CN106978201A (en) * | 2017-05-11 | 2017-07-25 | 张家港市昇泰能源有限公司 | A kind of vaporizing system charcoal boiler |
| RU180679U1 (en) * | 2018-03-12 | 2018-06-21 | Игорь Анатольевич Лагутин | CARBON BURNING FURNACE |
-
2006
- 2006-12-18 CN CNU2006200226155U patent/CN201031219Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105295969A (en) * | 2014-07-24 | 2016-02-03 | 北京南亚节能技术研究院 | Straw bio-energy preparation method |
| CN106978201A (en) * | 2017-05-11 | 2017-07-25 | 张家港市昇泰能源有限公司 | A kind of vaporizing system charcoal boiler |
| CN106978201B (en) * | 2017-05-11 | 2022-08-09 | 张家港市昇泰能源有限公司 | Gasification system charcoal boiler |
| RU180679U1 (en) * | 2018-03-12 | 2018-06-21 | Игорь Анатольевич Лагутин | CARBON BURNING FURNACE |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080305 Termination date: 20121218 |