CN102031151B - Anti-clogging biomass gasification combustor - Google Patents
Anti-clogging biomass gasification combustor Download PDFInfo
- Publication number
- CN102031151B CN102031151B CN 201010562123 CN201010562123A CN102031151B CN 102031151 B CN102031151 B CN 102031151B CN 201010562123 CN201010562123 CN 201010562123 CN 201010562123 A CN201010562123 A CN 201010562123A CN 102031151 B CN102031151 B CN 102031151B
- Authority
- CN
- China
- Prior art keywords
- combustion chamber
- chamber
- air
- escape pipe
- pipe
- 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.)
- Active
Links
Images
Landscapes
- Solid-Fuel Combustion (AREA)
- Incineration Of Waste (AREA)
Abstract
The invention provides an anti-clogging biomass gasification combustor. The combustor comprises a cavity and a hollow cylindrical combustion chamber, wherein the combustion chamber is communicated with a material feeding tube and an escape pipe; an air chamber is arranged between the cavity and the combustion chamber and is connected with an air pipe; the air pipe is connected with an air adjuster; and an air inlet is formed on the combustion chamber. Air enters the air chamber from the air pipe and then enters the combustion chamber from the air inlet to supplement the needed proper amount air and adjust the temperature in the combustion chamber. Because the air inlet amount of the air pipe is adjusted through the air adjuster, the air inlet amount can be reduced when the temperature in the combustion chamber is more than 1,000 DEG C; ash does not reach the melting point and avoid slagging because of the high temperature; the difficulty in cleaning solidified dregs is eased; and the disturbance on cyclone in the combustion chamber, which is caused by excessive deposited ash and does not contribute to cyclone dust removal, is eliminated.
Description
Technical field
The invention belongs to energy preparation field, specifically relate to a kind of combustion equipment of gasifying biomass.
Background technology
Along with the development of world economy, the energy and environmental problem become increasingly conspicuous.The human main energy sources of using at present has 3 kinds of oil, Sweet natural gas and coals.According to the International Energy Agency statistics, these 3 kinds of energy only have respectively about 35 years, 50 years and 240 years for the time limit of human exploitation on the earth.The fossil resources such as coal, oil exhaust the power supply constant tension day by day on the one hand; On the other hand, the excessive use of fossil resource has caused day by day serious environmental problem.Therefore, develop and seek new substitute energy and become the key subjects that human social must be solved in the new millennium.
Biomass energy is the sun power that is stored in by the photosynthesis of plant and sun power in the plant.According to estimates, 10 times of consuming in world's main fuel of the annual energy equivalence of storing of plant, and be less than 1% of its total amount as the utilization of the energy.The characteristics such as biomass material is because having the volatility height, and carbon is active high, and N, S content are low, and ash content is low are a kind of fuel of high-quality.By the biomass energy switch technology, can utilize efficiently this reproducible clean biomass energy, the fuel such as Substitute coal, oil and natural gas.
At present, utilize biomass material, such as straw, bagasse, rice chaff, sawdust, wood chip etc., it is carried out middle temperature or high temperature pyrolysis after, can extract bio-oil or biological fuel gas.And existing combustion technology mainly is fire grate grate firing burning and fluidized bed combustion, wherein, adopting the shortcoming of fire grate grate firing enamelware pot is that fuel combustion is incomplete, thermo-efficiency is low, adopt under the burning or pyrolytical condition of high temperature having to, and the ash that produces (silicon-dioxide and some metal-salts) is surpassing easily slagging scorification in 1000 ℃ the situation, the accumulated slag amount is as too much, can stop up the combustion chamber, affect combustion efficacy.And the employing fluid-bed combustion furnace generally only is to be applied to large-sized boiler, and its investment is huge, and production cost is high, can not try hard to recommend greatly application in medium-sized and small enterprises.
Summary of the invention
The problem that exists in order to solve prior art the invention provides a kind of biomass burner that can prevent the biomass ash slagging scorification.
Technical scheme of the present invention is as follows: burner of the present invention, comprise cavity, the throat less chamber of hollow, the combustion chamber is communicated with feed-pipe and escape pipe, has air chamber between described cavity and the combustion chamber, and described air chamber is connected with airduct, described airduct connects ventilating regulator, an intake opening has been opened in described combustion chamber, and wind enters air chamber from airduct and enters the combustion chamber through intake opening, to replenish required proper amount of gas and the combustion chamber internal temperature is regulated.
The axial inwall of described intake opening and the cross section inwall of combustion chamber are tangent, and the wind of air chamber tangentially enters the combustion chamber from intake opening, and the self-forming whirlwind carries out centrifugation to ash.
Described escape pipe is horizontally set at the center of combustion chamber, and the left end of escape pipe places the combustion chamber to be built-in end, and the right-hand member of escape pipe stretches out and is external part outside the combustion chamber.
The tube wall of the built-in end of described escape pipe is provided with some through holes.
Described escape pipe is horizontally set at the center of combustion chamber, and the entrance of escape pipe is connected with the outlet of combustion chamber.
Described air chamber is provided with dividing plate, and dividing plate is divided into secondary air chamber and tertiary chamber with air chamber, and described airduct is comprised of secondary air channel and tertiary-air pipe; Described secondary air chamber is connected with secondary air channel, the entrance of secondary air channel connects ventilating regulator, described combustion chamber offers an intake opening, the axial inwall of described intake opening and the cross section inwall of combustion chamber are tangent, wind enters air compartment from secondary air channel and tangentially enters the combustion chamber through intake opening, and the self-forming whirlwind replenishes required air for the combustion chamber and the combustion chamber internal temperature is regulated; Described tertiary chamber is connected with tertiary-air pipe; The tube wall of the external part of described escape pipe offers production well; Described tertiary chamber is communicated with production well.
The outer setting of described cavity has thermal insulation layer, and the main body of described combustion chamber is flame retardant coating.
Also comprise lighter for ignition and explosive door.
Described burner offers fire door, and described fire door is equipped with bell, and the top of described fire door arranges form.
Also include the base that can make burner move or load and unload, for detection of the detection means of temperature.
The present invention is owing to be provided with air compartment, the oxygen of timely aftercombustion chamber, simultaneously, the air output of airduct is regulated by ventilating regulator, when the temperature of combustion chamber surpasses 1000 ℃, can reduce air output, make lime-ash can not reach molten point and slagging scorification by Yin Gaowen, both alleviated the difficulty of cleaning slagging scorification, eliminated again because depositing too much lime-ash the combustion chamber internal cyclone is formed to disturb be unfavorable for cyclone ash removal.
In addition, because wind tangentially enters in the columnar combustion chamber from blast pipe or intake opening, can the self-forming whirlwind, the ash of biological fuel gas is separated.This structure, the biogas of making does not need separately ash disposal, has reduced processing step, has saved the time for preparing clean biological fuel gas, has also saved ash handling equipment, has reduced production cost.
Description of drawings
Fig. 1 is the internal structure of burner of the present invention;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 is the left view of Fig. 1;
Fig. 4 is the structural relation synoptic diagram of feed-pipe and combustion chamber;
Fig. 5 is the structural relation synoptic diagram of intake opening and combustion chamber;
Fig. 6 is the cross sectional representation of escape pipe.
Embodiment
This burner is heat-storage type burner, and the diameter of combustion chamber is 0.8m, and capacity is 0.75.As Figure 1-3, this burner is comprised of base 12, cavity 20, thermal insulation layer 11, flame retardant coating 9, lighter for ignition 18, feed-pipe 15, secondary air channel 19, dividing plate 5, tertiary-air pipe 17, escape pipe 8, bell 10, form 1 and explosive door 13.The burner body structure supports fixing by base 12.Cavity 20 is hollow circle tube, the accumbency setting.The inside of cavity 20 is provided with flame retardant coating 9, and this flame retardant coating 9 also is the hollow cylinder structure.The hollow cylinder structure of flame retardant coating 9 has formed combustion chamber 2.Combustion chamber 2 is communicated with the axial inwall of this feed-pipe 15 and the lateral cross section inwall of combustion chamber 2 tangent (such as Fig. 4) with the feed-pipe 15 that cavity 20 arranges.The inwall of the outer wall of flame retardant coating 9 and cavity 20 has the space, and this space has formed air compartment.The inside of cavity 20 and in the left side of flame retardant coating 9 is provided with thermal insulation layer 11.The left end of combustion chamber 2 is provided with a fire door, and by bell 10 sealings.Be positioned at the top of fire door, also be provided with a form 1, be used for observing the combustion case in the burner, the unusual phenomenon when in time finding burning.The axis direction of combustion chamber 2 and be positioned at right side place arranged transversely one escape pipe 8 of combustion chamber 2, escape pipe 8 and combustion chamber 2 concentric settings, this escape pipe 8 is the direct piping of both ends open, the diameter of pipeline is 0.4m.It is built-in end that the left end of escape pipe 8 inserts in 2 inside, combustion chamber, the distance of the inner left wall of the left port of built-in end and combustion chamber 2 is 500mm, the right-hand member of escape pipe 8 extends outside the combustion chamber 2 and exposes to outside the cavity 20 is external part, and the external part of escape pipe 8 is connected with the entrance of boiler (not shown).The external part tube wall of escape pipe 8 offers 8 and discharges pore 16(such as Fig. 6), every discharge pore 16 is evenly arranged on the cross section of escape pipe 8, and the quantity of every discharge pore 16 is 3, and production well 16 is communicated with tertiary chamber 6.Space between the inwall of the outer wall of flame retardant coating 9 and cavity 20 has formed air compartment, be divided into secondary air chamber 4 and tertiary chamber 6, secondary air chamber 4 and tertiary chamber 6 are separated by dividing plate 5, and dividing plate also plays the effect of supporting the combustion chamber except forming secondary air chamber 4 and tertiary chamber 6.The outside connecting secondary airduct 19 of secondary air chamber 4, the entrance of secondary air channel 19 connects ventilating regulator, and ventilating regulator can be chosen butterfly valve (not shown) etc.One intake opening 14 is set, the axial inwall of this intake opening 14 and the lateral cross section inwall of combustion chamber 2 tangent (such as Fig. 5) between secondary air chamber 4 and the combustion chamber 2.The outside of tertiary chamber 6 connects tertiary-air pipe 17.Burner is provided with lighter for ignition 18, when working first, utilizes coal gas ignition that the combustion chamber is risen 400 ℃, then begins the whirlwind charging.Also be provided with temperature detection device in the combustion chamber 2, can be thermopair 3, be used for measuring the furnace temperature of combustion chamber, generally surpass 1000 ℃ and namely report to the police.Open bell 10 and just can conveniently be combustion chamber 2 interior cleaning lime-ash.Base 12 can make things convenient for dismounting and the movement of burner.Explosive door 13 is in order to prevent the burner hypertonia, when internal pressure of combustion chamber surpasses 0.01Mpa, opens the explosive door relief pressure, can prevent superpressure and blasts and cause Peril Incident.
The working process of burner is as follows: at first initial igniter 18, after the burning room temp reaches more than 400 ℃, biomass material is after crushed tangentially blown into combustion chamber 2 from feed-pipe 15 by a wind, interiorly in combustion chamber 2 forms biological fuel gas and some biomass ashs (such as silicon-dioxide and metal-salt etc.) after through 1 to 2 second high temperature (900～1000 ℃) gasification, and combustion.In combustion processes, because a wind is tangentially to enter the combustion chamber, therefore can be at columnar combustion chamber 2 interior formation whirlwind, under the centrifugal action of whirlwind, the grey separated and lower bottom that is sunken to the combustion chamber that burning generates, the clean biological fuel gas of combustion chamber 2 axis centre then enters in the boiler by escape pipe 8.Simultaneously, 19 pairs of secondary air chambers of secondary air channel 4 continue air-supply, and enter combustion chamber 2 by intake opening 4 tangential air-supplies, form whirlwind with the required oxygen of aftercombustion chamber 2 interior gasification incomplete combustions.Through burning after a while, if the temperature in the combustion chamber 2 surpasses 1000 ℃, then can reach fusion point of ash and easily slagging scorification.After thermopair 3 detects too high temperature, reduce the air quantity that enters secondary air chamber 4 with butterfly valve control, thereby reduce the combustion chamber amount of oxygen, be lower than 1000 ℃ to guarantee the burning room temp.Before clean biological fuel gas enters boiler, also biological fuel gas is replenished air (oxygen), namely tertiary air enters tertiary chamber from tertiary-air pipe 17, mixes with biological fuel gas by tertiary air, make together to enter in the boiler fully burning, to obtain the boiler of feeding more heat that burns.
Claims (10)
1. Anti-slagging biomass gasifying burner, comprise cavity, the throat less chamber of hollow, combustion chamber are communicated with feed-pipe and escape pipe, it is characterized in that, has air chamber between described cavity and the combustion chamber, described air chamber is connected with airduct, and described airduct connects ventilating regulator, and an intake opening has been opened in described combustion chamber, wind enters air chamber from airduct and enters the combustion chamber through intake opening, to replenish required proper amount of gas and the combustion chamber internal temperature is regulated.
2. burner according to claim 1 is characterized in that, the axial inwall of described intake opening and the cross section inwall of combustion chamber are tangent, and the wind of air chamber tangentially enters the combustion chamber from intake opening, and the self-forming whirlwind carries out centrifugation to ash.
3. burner according to claim 1 and 2 is characterized in that, described escape pipe is horizontally set at the center of combustion chamber, and the left end of escape pipe places the combustion chamber to be built-in end, and the right-hand member of escape pipe stretches out and is external part outside the combustion chamber.
4. burner according to claim 3 is characterized in that, the tube wall of the built-in end of described escape pipe is provided with some through holes.
5. burner according to claim 1 is characterized in that, described escape pipe is horizontally set at the center of combustion chamber, and the entrance of escape pipe is connected with the outlet of combustion chamber.
6. burner according to claim 3 is characterized in that, described air chamber is provided with dividing plate, and dividing plate is divided into secondary air chamber and tertiary chamber with air chamber, and described airduct is comprised of secondary air channel and tertiary-air pipe; Described secondary air chamber is connected with secondary air channel, the entrance of secondary air channel connects ventilating regulator, described combustion chamber offers an intake opening, the axial inwall of described intake opening and the cross section inwall of combustion chamber are tangent, wind enters air compartment from secondary air channel and tangentially enters the combustion chamber through intake opening, and the self-forming whirlwind replenishes required air for the combustion chamber and the combustion chamber internal temperature is regulated; Described tertiary chamber is connected with tertiary-air pipe; The tube wall of the external part of described escape pipe offers production well; Described tertiary chamber is communicated with production well.
7. burner according to claim 1 is characterized in that, the outer setting of described cavity has thermal insulation layer, and the main body of described combustion chamber is flame retardant coating.
8. burner according to claim 1 is characterized in that, also comprises lighter for ignition and explosive door.
9. burner according to claim 1 is characterized in that, described burner offers fire door, and described fire door is equipped with bell, and the top of described fire door arranges form.
10. burner according to claim 1 is characterized in that, also includes the base that can make burner move or load and unload, for detection of the detection means of temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010562123 CN102031151B (en) | 2010-11-25 | 2010-11-25 | Anti-clogging biomass gasification combustor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010562123 CN102031151B (en) | 2010-11-25 | 2010-11-25 | Anti-clogging biomass gasification combustor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102031151A CN102031151A (en) | 2011-04-27 |
| CN102031151B true CN102031151B (en) | 2013-03-20 |
Family
ID=43884615
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010562123 Active CN102031151B (en) | 2010-11-25 | 2010-11-25 | Anti-clogging biomass gasification combustor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102031151B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102588951A (en) * | 2012-03-21 | 2012-07-18 | 德清县华恒涂装设备有限公司 | Biomass burner |
| CN103925593A (en) * | 2013-01-16 | 2014-07-16 | 戴增池 | Efficient biomass vortex burner |
| CN103436295B (en) * | 2013-08-09 | 2016-05-04 | 张冰娃 | Biomass fuel is produced the method for combustible gas |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2476716Y (en) * | 2001-04-16 | 2002-02-13 | 张德地 | Gasification combustion stove using solid fuel |
| CN201181013Y (en) * | 2008-03-26 | 2009-01-14 | 娄劲松 | Air suction type gasification furnace |
| CN201857369U (en) * | 2010-11-25 | 2011-06-08 | 广州迪森热能技术股份有限公司 | Anti-slagging biomass gasifying burner |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU2008327957B2 (en) * | 2007-11-19 | 2011-07-21 | Shell Internationale Research Maatschappij B.V. | Process to prepare a mixture of hydrogen and carbon monoxide |
-
2010
- 2010-11-25 CN CN 201010562123 patent/CN102031151B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2476716Y (en) * | 2001-04-16 | 2002-02-13 | 张德地 | Gasification combustion stove using solid fuel |
| CN201181013Y (en) * | 2008-03-26 | 2009-01-14 | 娄劲松 | Air suction type gasification furnace |
| CN201857369U (en) * | 2010-11-25 | 2011-06-08 | 广州迪森热能技术股份有限公司 | Anti-slagging biomass gasifying burner |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102031151A (en) | 2011-04-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202322753U (en) | Downdraft biomass fuel gasifier | |
| CN201526953U (en) | Biomass gasified combustion coupling cyclone boiler | |
| CN101812327B (en) | Down-draught type biomass gasifier for secondarily cracking tar | |
| CN102010755B (en) | Biomass vaporizing burner adopting cyclone dust-removing method | |
| CN201857369U (en) | Anti-slagging biomass gasifying burner | |
| CN103644562A (en) | Combined type energy-saving biomass fuel boiler | |
| CN102031151B (en) | Anti-clogging biomass gasification combustor | |
| CN205528623U (en) | Family is with type living beings gas generation system | |
| CN201081254Y (en) | Household biomass gasification stove | |
| CN203923114U (en) | External burner biomass gasifying furnace | |
| CN201926118U (en) | Heat transfer oil furnace and vortex combustor biomass all-in-one machine | |
| CN101993732B (en) | Vaporizing combustion chamber of high-energy biomasses | |
| CN210796370U (en) | Multilayer gas emission device | |
| CN102676235A (en) | Downdraft tar secondary pyrolysis gasification device | |
| CN201923985U (en) | Cyclone ash removal biomass gasification combustor | |
| CN201915070U (en) | Gasification combustor for high-energy biomass | |
| CN201059621Y (en) | Integral home-use biomass gas producing furnace | |
| CN202521589U (en) | Horizontally-blown heat energy generator for solid fuels | |
| CN105838446A (en) | Household biomass gas generation system | |
| CN207334717U (en) | Energy-saving biological fuel apparatus | |
| CN102032672B (en) | Biomass integrated machine consisting of heat conducing oil furnace and cyclone burner | |
| CN201926108U (en) | Biomass vertical heat-conducting oil furnace | |
| CN218763447U (en) | Environment-friendly biomass industrial gasification furnace | |
| CN103980945B (en) | External burner biomass gasifying furnace and biomass gasification method | |
| CN202626125U (en) | Downdraft tar secondary cracking gasification device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Anti slagging biomass gasification burner Effective date of registration: 20220401 Granted publication date: 20130320 Pledgee: Agricultural Bank of China Limited Guangzhou Liuhua sub branch Pledgor: GUANGZHOU DEVOTION THERMAL TECHNOLOGY Co.,Ltd. Registration number: Y2022980003837 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |