CN201180123Y - Semiwater gas generating stove for solid biomass - Google Patents
Semiwater gas generating stove for solid biomass Download PDFInfo
- Publication number
- CN201180123Y CN201180123Y CNU2008200323046U CN200820032304U CN201180123Y CN 201180123 Y CN201180123 Y CN 201180123Y CN U2008200323046 U CNU2008200323046 U CN U2008200323046U CN 200820032304 U CN200820032304 U CN 200820032304U CN 201180123 Y CN201180123 Y CN 201180123Y
- Authority
- CN
- China
- Prior art keywords
- slag
- gasification
- heater
- flame retardant
- solid biomass
- 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
- 239000002028 Biomass Substances 0.000 title claims abstract description 12
- 239000007787 solid Substances 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000011248 coating agent Substances 0.000 claims abstract description 12
- 238000000576 coating method Methods 0.000 claims abstract description 12
- 239000003063 flame retardant Substances 0.000 claims abstract description 12
- 239000002893 slag Substances 0.000 claims abstract description 12
- 230000005540 biological transmission Effects 0.000 claims abstract description 9
- 239000000498 cooling water Substances 0.000 claims abstract description 5
- 239000003818 cinder Substances 0.000 claims description 17
- 239000000126 substance Substances 0.000 claims description 7
- 210000003205 muscle Anatomy 0.000 claims description 6
- 238000007670 refining Methods 0.000 claims description 6
- 238000007689 inspection Methods 0.000 claims description 5
- 239000004744 fabric Substances 0.000 claims description 4
- 238000009413 insulation Methods 0.000 claims description 4
- 230000008676 import Effects 0.000 claims description 3
- 239000003034 coal gas Substances 0.000 claims description 2
- 238000010079 rubber tapping Methods 0.000 claims description 2
- 238000002309 gasification Methods 0.000 abstract description 16
- 239000000463 material Substances 0.000 abstract description 8
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 230000007246 mechanism Effects 0.000 abstract description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 239000003795 chemical substances by application Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract description 2
- 230000008569 process Effects 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 16
- 239000000567 combustion gas Substances 0.000 description 6
- 238000006722 reduction reaction Methods 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000036760 body temperature Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000001535 kindling effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
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- Solid-Fuel Combustion (AREA)
Abstract
The utility model provides a solid biomass semi-water gas generating furnace, comprising a furnace body, a transmission mechanism, a feeding mechanism and a deslagging mechanism, wherein the inside of the furnace body (1) is provided with an insulating course (2) and a flame retardant coating (3), the inside of the flame retardant coating (3) is provided with a heat exchanging pipe (4), a hearth is provided with a material revolving harrow (7); the lower part of the furnace body (1) is provided with a slag cabin (12) and a cooling water tank (13), the slag cabin (12) is provided with a gasifying agent inlet (14), the bottom of the slag cabin (12) is provided with a slag outlet (15) and is connected with a spiral slag discharging device (17); and interface of the hearth and the slag cabin (12) is provided with a rotational grate bar (18). The solid biomass semi-water gas generating furnace is fed and discharges slag continuously, guarantees the continuity and the stability of the gasification process, adopts the afterheat to generate water vapor to perform the gasification reaction, improves the utilization rate of the carbon element, improves the rate of gasification of the solid biomass, increases the gasification intensity by 1.5 to 2.0 times compared with the gasification furnace with the same cross section, and increases the thermal value of flammable gas about one time.
Description
One, technical field
The utility model relates to a kind of chemical industry equipment, particularly a kind of energy converting apparatus, and specifically a kind of is the producer of raw material generation semi-water gas with the low density solid biomass.
Two, background technology
Agricultural solid waste such as low-density stalk is existing multiple through the equipment that pyrolytic gasification is converted into geseous fuel.But the vapourizing furnace that puts goods on the market at present owing to characteristics such as the energy resource density of solid biologic are low, and bulk density is little, causes the vapourizing furnace gasification intensity low, and gasification efficiency is low, and fuel gases calorific value is low.Be 900N in the maximum gas production rate of the fixed-bed type vapourizing furnace of operation at present
3/ h, calorific value are 1000～1100kcae/N m
3Thereby the range of application of restriction vapourizing furnace.
Three, summary of the invention
Producer provided by the utility model is intended to use low-density solid biomass production high quality gas fuel, and problem to be solved is that semi-water gas takes place.
This producer has been used for reference the principle of blue-gas generator, designs in conjunction with the characteristics of solid biomass (calling material in the following text).Concrete technical scheme comprises the slagging device of transmission rig, feed mechanism and its below of body of heater 1 and top thereof, at body of heater 1 inwall thermal insulation layer 2 and flame retardant coating 3 is arranged, and the surface of flame retardant coating 3 is a curved surface, and this curved surface is " girdling the waist " shape in the middle of making burner hearth, as shown in Figure 1." girdling the waist " is divided into two portions up and down with burner hearth, and as shown in phantom in Figure 1, " girdling the waist " is the place that the energy transforms with the burner hearth on top, and promptly material is finished a series of chemical processes such as oxidation, reduction, conversion and gasified; " girdle the waist " with the lower section is ash bed.Be provided with spiral heat exchange tube 4 in the flame retardant coating 3, be intended to make full use of the heat energy in the burner hearth, produce water vapour, return burner hearth generation semi-water gas after water vapour and the air mixed again.Body of heater 1 is provided with semi-water gas outlet 5 and inspection port 6.Be provided with dentation refining rake 7 on the top of burner hearth, its effect is with the even cloth of the material that is added by feeding screw 11 and rolls to improve its density that refining rake 7 is driven by transmission rig, and transmission rig is made up of motor 8, speed reduction unit 9 and axle 10.
The below of body of heater 1 is connected with cinder tank 12, it is outside equipped with cooling water tank 13, vaporized chemical import 14 is arranged on the cinder tank 12, so-called vaporized chemical is meant the mixed gas of air or air and water vapour, lime-ash outlet 15 is arranged at cinder tank 12 bottoms, and lime-ash outlet 15 connects with spiral slag off apparatus 17 and controlled by valve 16.
This producer is operation like this and operation:
Before the igniting preliminary stalk ash is dropped in the stove the about 50cm of floor height by inspection port 6.Then kindling material is dropped on the ash bed from inspection port 6; Solid biomass after giving processing is pushed in the burner hearth by feed auger 11; Start gas blower vaporized chemical (air is or/and the gas mixture of water vapour) is blasted burner hearth, lower floor's biological particles initial burning burning, and heating furnace body and upper materials, body of heater is again with the spiral heat exchange tube 4 in the part heat transferred flame retardant coating 3; The control oxygen-supplying amount gasifies biomass under the insufficient condition of oxygen supply, produce inflammable gas, and inflammable gas is purified the back and supplied with the user by air outlet 5 input gas-purification systems.
Solid biomass generates lime-ash at last through super-dry, restoring transformation, oxidation from top to bottom.The inflammable gas that the igniting initial stage produces is based on CO, after treating that furnace body temperature raises, the water vapour that is produced by spiral heat exchange tube 4 is able to preheating when going into ash bed through cinder tank 12, grate 18 are laggard successively with air mixed, improved gasification agent temperature, reduced cindery temperature simultaneously, in oxidation, reduction reaction, water vapour and CO
2Metallic element katalysis down conversions such as silicon, iron, aluminium are H in lime-ash
2And CH
4, make inflammable gas improve calorific value and quality.
Lime-ash after the gasification, the grate 18 that is rotated are radially passed and are fallen into cinder tank 12; Cinder tank 12 peripheral hardware cooling water tanks 13 are used to reclaim the lime-ash waste heat, gained hot water supply spiral heat exchange tube 4; Cooled lime-ash is discharged by valve 16, slag tapping equipment 17.
This producer is compared with conventional device, and following advantage is arranged: in (1) raw material input stove, be covered with furnace profile under the effect of refining rake 7, and rolled, improved density and rate of heat transfer.Material drying, restoring transformation, is oxidized to lime-ash in folding process.(2) Xuan Zhuan taper type grate 18 can continuously be removed lime-ash, thereby has guaranteed the stability of gasification bed, helps improving the continuity of combustion gas quality and production.(3) UTILIZATION OF VESIDUAL HEAT IN and CO to greatest extent
2The conversion inflammable gas is another characteristics of this vapourizing furnace.Utilize body of heater inner member and lime-ash waste heat to improve gasification temperature, thereby improved the zone of oxidation temperature, strengthened gasification intensity, improved material gasification rate and combustion gas quality; Cooling body of heater and the water vapour that produces participates in reaction, in lime-ash under the katalysis of metallic element, the CO that gasification is generated
2Be transformed into H
2, CH
4, so not only made full use of the carbon in the raw material, reduce the proportion of CO in combustion gas, and improved fuel gases calorific value, improved the security that combustion gas is used.In addition, the Seal Design of each running gear has prevented the infiltration of air, has reduced the oxygen level of combustion gas, also helps improving the security that combustion gas is used.This producer is compared with the vapourizing furnace with the cross section, and gasification intensity improves 1.5～2.0 times, and fuel gases calorific value can be mentioned 2000kcae/N m
3More than.
Four, description of drawings
Fig. 1 is a structural representation of the present utility model.The flow direction of filled arrows signal solid materials, lime-ash and water coolant among the figure, hollow arrow is the flow direction of gas.
Fig. 2, Fig. 3 are the structural representations of grate 18, and wherein Fig. 3 is the vertical view of Fig. 2, and three spiral muscle 24 are arranged on the conical surface 22.
Five, embodiment
1, gets the cylindric body of heater 1 that steel plate processing has pneumatic outlet 5 and inspection port 6, at body of heater 1 internal fixing thermal insulation layer 2, fixing flame retardant coating 3 on the thermal insulation layer 2, flame retardant coating 3 internal surfaces are cambered surface, this cambered surface makes the burner hearth middle part be " girdling the waist " shape, is preset with spiral heat exchange tube 4. in flame retardant coating 3
2, feeding screw 11 is set above body of heater 1, speed reduction unit 9 and motor 8 are set simultaneously, harrow 7 with high temperature steel processing dentation refining, and be connected on the speed reduction unit 9 by axle 10, refining rake 7 is positioned at the top of burner hearth.
3, with steel plate processing awl bucket shape cinder tank 12, vaporized chemical import 14 is arranged on it, its awl bucket part is connected with cooling water tank 13.Lime-ash outlet 15 is arranged at cinder tank 12 bottoms, and matches with valve 16.
4, rotation grate 18 be integrated poured moulding, comprises the skeleton 21 of be with cross bracing and three spiral muscle that show unique characteristics 24, and three special-shaped panels formation conical surfaces 22 (cast iron) of support are processed with wind distributing hole 23 on the muscle width of cloth on it.
5, grate 18 is fixed to the below of body of heater 1 after cinder tank 12 tops cooperate, spiral slag off apparatus 17 is connected with lime-ash outlet 15.
Claims (3)
1, a kind of solid biomass semi-water coal-gas producer, the cinder tank (12), the spiral slag tapping equipment (17) that comprise transmission rig, feeding screw (11) and its below of the body of heater (1) that can constitute burner hearth and top thereof, it is characterized in that: thermal insulation layer (2) and flame retardant coating (3) are arranged at body of heater (1) inwall, the surface of flame retardant coating (3) is a curved surface, this curved surface makes the burner hearth middle part be " girdling the waist " shape, and spiral heat exchange tube (4) is arranged in the flame retardant coating (3); Semi-water gas outlet (5) and inspection port (6) are arranged on the body of heater (1); The dentation refining rake (7) that the promising transmission rig of upper furnace that is made of body of heater (1) drives; Be connected with cinder tank (12) in body of heater (1) below, cinder tank (12) is outside equipped with cooling water tank (13), vaporized chemical import (14) is arranged on the cinder tank (12), and lime-ash outlet (15) is arranged at cinder tank (12) bottom, valve (16) is arranged on it and connects with spiral slag off apparatus (17); Be provided with the grate (18) that matches with transmission conical gear (19) and roller (20) at the interface at cinder tank (12) and burner hearth.
2, producer according to claim 1 is characterized in that: described grate (18) is made up of the annular skeleton (21) that cross bracing is arranged and the last fixed conical surface (22) thereof, and the wind distributing hole (23) and the spiral muscle width of cloth (24) are arranged on the conical surface (22).
3, producer according to claim 1 and 2 is characterized in that: three spiral muscle width of cloth (24) are arranged on the described grate (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200323046U CN201180123Y (en) | 2008-02-29 | 2008-02-29 | Semiwater gas generating stove for solid biomass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200323046U CN201180123Y (en) | 2008-02-29 | 2008-02-29 | Semiwater gas generating stove for solid biomass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201180123Y true CN201180123Y (en) | 2009-01-14 |
Family
ID=40249622
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200323046U Expired - Fee Related CN201180123Y (en) | 2008-02-29 | 2008-02-29 | Semiwater gas generating stove for solid biomass |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201180123Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101955798A (en) * | 2010-09-02 | 2011-01-26 | 蓝星化工有限责任公司 | Water gas producer |
| CN102121706A (en) * | 2010-10-26 | 2011-07-13 | 上海交通大学 | Biomass gasifying and reburning system for coal-fired boiler |
| CN102329656A (en) * | 2011-08-30 | 2012-01-25 | 张建超 | Downdraft biomass gasification reaction chamber and gasification process thereof |
-
2008
- 2008-02-29 CN CNU2008200323046U patent/CN201180123Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101955798A (en) * | 2010-09-02 | 2011-01-26 | 蓝星化工有限责任公司 | Water gas producer |
| CN102121706A (en) * | 2010-10-26 | 2011-07-13 | 上海交通大学 | Biomass gasifying and reburning system for coal-fired boiler |
| CN102121706B (en) * | 2010-10-26 | 2012-12-26 | 上海交通大学 | Biomass gasifying and reburning system for coal-fired boiler |
| CN102329656A (en) * | 2011-08-30 | 2012-01-25 | 张建超 | Downdraft biomass gasification reaction chamber and gasification process thereof |
| CN102329656B (en) * | 2011-08-30 | 2013-06-05 | 张建超 | Downdraft biomass gasification reaction chamber and gasification process thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Solid biomass semi-water coal-gas producer Effective date of registration: 20110922 Granted publication date: 20090114 Pledgee: Anhui Province Anhui investment credit Company Limited by Guarantee Pledgor: Hefei Tianyan Exploitation of Green Energy Sources Co., Ltd. Registration number: 2011990000369 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20120910 Granted publication date: 20090114 Pledgee: Anhui Anhui Investment & financing Company Limited by Guarantee Pledgor: Hefei Tianyan Exploitation of Green Energy Sources Co., Ltd. Registration number: 2011990000369 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Solid biomass semi-water coal-gas producer Effective date of registration: 20120910 Granted publication date: 20090114 Pledgee: Anhui Anhui Investment & financing Company Limited by Guarantee Pledgor: Hefei Tianyan Exploitation of Green Energy Sources Co., Ltd. Registration number: 2012990000513 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PM01 | Change of the registration of the contract for pledge of patent right |
Change date: 20120910 Registration number: 2011990000369 Pledgee after: Anhui Anhui Investment & financing Company Limited by Guarantee Pledgee before: Anhui Province Anhui investment credit Company Limited by Guarantee |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20130918 Granted publication date: 20090114 Pledgee: Anhui Anhui Investment & financing Company Limited by Guarantee Pledgor: Hefei Tianyan Exploitation of Green Energy Sources Co., Ltd. Registration number: 2012990000513 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Solid biomass semi-water coal-gas producer Effective date of registration: 20131024 Granted publication date: 20090114 Pledgee: Anhui Anhui Investment & financing Company Limited by Guarantee Pledgor: Hefei Tianyan Exploitation of Green Energy Sources Co., Ltd. Registration number: 2013990000774 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20140116 Granted publication date: 20090114 Pledgee: Anhui Anhui Investment & financing Company Limited by Guarantee Pledgor: Hefei Tianyan Exploitation of Green Energy Sources Co., Ltd. Registration number: 2013990000774 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| ASS | Succession or assignment of patent right |
Owner name: HEFEI TIANYAN BIOMASS ENERGY TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: TIANYAN GREEN ENERGY DEVELOPMENT CO., LTD., HEFEI Effective date: 20140129 |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: HEFEI, ANHUI PROVINCE TO: 230601 HEFEI, ANHUI PROVINCE |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20140129 Address after: 230601 Anhui city of Hefei Province Economic and Technological Development Zone Cuiwei Road No. 6 building five floor 514 constant sea Patentee after: Hefei Tianyan Biomass Technology Co. Ltd. Address before: Luyang District of Hefei City, Anhui Province, Yang big national high-tech Forestry Park Patentee before: Hefei Tianyan Exploitation of Green Energy Sources Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090114 Termination date: 20150229 |
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| EXPY | Termination of patent right or utility model |