CN202902605U - Biomass fuel inverse combustion boiler - Google Patents
Biomass fuel inverse combustion boiler Download PDFInfo
- Publication number
- CN202902605U CN202902605U CN 201220621176 CN201220621176U CN202902605U CN 202902605 U CN202902605 U CN 202902605U CN 201220621176 CN201220621176 CN 201220621176 CN 201220621176 U CN201220621176 U CN 201220621176U CN 202902605 U CN202902605 U CN 202902605U
- Authority
- CN
- China
- Prior art keywords
- water
- boiler
- combustion
- combustion chamber
- fuel
- Prior art date
Links
- 238000002485 combustion reactions Methods 0.000 title claims abstract description 58
- 239000000446 fuels Substances 0.000 title claims abstract description 28
- 239000002028 Biomass Substances 0.000 title claims abstract description 19
- 239000011901 water Substances 0.000 claims abstract description 30
- 239000010410 layers Substances 0.000 claims abstract description 24
- 239000007789 gases Substances 0.000 claims abstract description 19
- 241000005139 Lycium andersonii Species 0.000 claims abstract description 12
- 239000003570 air Substances 0.000 claims abstract description 6
- 238000001816 cooling Methods 0.000 claims abstract description 4
- 239000000779 smoke Substances 0.000 abstract description 5
- 125000004122 cyclic group Chemical group 0.000 abstract description 3
- 238000002309 gasification Methods 0.000 abstract 1
- AHKZTVQIVOEVFO-UHFFFAOYSA-N oxide(2-) Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [O-2] AHKZTVQIVOEVFO-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering processes Methods 0.000 description 3
- 229910001890 sulfur dioxide Inorganic materials 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound 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O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000003546 flue gases Substances 0.000 description 2
- 239000002737 fuel gases Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 239000000126 substances Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 1
- 239000000470 constituents Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003138 indicators Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000007254 oxidation reactions Methods 0.000 description 1
- 230000000505 pernicious Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000007787 solids Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
Abstract
The utility model relates to a biomass fuel inverse combustion boiler which comprises a boiler body, a smoke outlet arranged on the boiler body, a water level gauge, a furnace hearth formed in the boiler body, a cooling grate arranged on the lower portion of the furnace hearth, and a water jacket, a water inlet, and a water outlet, wherein the water jacket, the water inlet, and the water outlet are arranged on the periphery of the furnace hearth. The smoke outlet is connected with an induced draft fan. The biomass fuel inverse combustion boiler is characterized in that a water layer wall is arranged on the furnace hearth, the water layer wall is in a Z-shaped structure, the furnace hearth is divided into an upper convection heat exchange chamber and a lower combustor by the water layer wall, a gas combustion chamber is formed in the side wall of the combustor, the upper portion of the gas combustion chamber is communicated with the smoke outlet through the convection heat exchange chamber, the lower portion of the gas combustion chamber is communicated with lower end of the combustor, the water layer wall is communicated with the water jacket, and the air inlet of the water layer wall is arranged on the side wall of the boiler body. The biomass fuel inverse combustion boiler has the advantages that the structure is simple, and thermal efficiency is high; and with fuel inverse combustion, gasification and combustion are integrated, fuel cyclic combustion layer by layer in the combustor is realized, thermal efficiency of the fuel is high, and the biomass fuel inverse combustion boiler is an ideal device to use biomass energy.
Description
Technical field
The utility model belongs to the boiler technology field, relates in particular to a kind of biomass fuel reverse combustion type boiler.
Background technology
Boiler is thermal power transfer equipment, also is pollution sources simultaneously.Thermal efficiency height and pollution level are to weigh two important indicators of boiler.Traditional boiler structure normally is comprised of pot and stove.Topmost parts are burner hearth and boiler drum in the boiler body.Burner hearth claims again the combustion chamber, its structures shape combustion system and used fuel, be the major part that determines the thermal efficiency and pollution.Because they all are to adopt the positive theory of combustion, mostly take coal as fuel, in combustion process, produce a large amount of pernicious gas contaminated environment such as sulfur dioxide, and the thermal efficiency is low, generally about 80%.
Because coal resources worsening shortages; countries in the world all utilize technology carrying out biomass combustion; to solve the problem that energy crisis was produced, well-known, living beings are discarded objects of agricultural, production of forestry; if abandon arbitrarily burning; the meeting serious environment pollution utilizes living beings to burn in boiler, and the steam that produces is used for generating or steam supply; social benefit with energy savings, environmental contamination reduction also has good economic benefit.
At present, oneself boiler of the biological substance for combustion through releasing all is to research and develop in the technical foundation of coal-burning boiler.But, because biomass fuel moisture content is large, volatilization point is low, fugitive constituent is many, energy density is low, the boiler product of the biological substance for combustion of energy practical application all is again supporting gas-fired stove tool burning after employing fluidized bed combustion or the vaporization, this dual mode, system complex, investment is large, is difficult for realizing miniaturization, does not all reach desirable degree.
Summary of the invention
The purpose of this utility model provides a kind of sufficient combustion, and the thermal efficiency is high, and is simple to operate, the biomass fuel reverse combustion type boiler of environmental protection.
The purpose of this utility model realizes by following technical proposals:
Biomass fuel reverse combustion type boiler of the present utility model, comprise body of heater, be arranged on the exhaust opening on the body of heater, limnimeter, be arranged on the burner hearth in the body of heater, be arranged on the cooling fire grate of lower furnace portion and the water jacket that is arranged on the burner hearth periphery, water inlet pipe and outlet pipe, described exhaust opening is connected with air-introduced machine, it is characterized in that in described burner hearth, being provided with the water layer wall, described water layer wall is Z-shaped structure, and burner hearth is divided into top convection heat-exchange chamber and lower combustion chamber, and form the gas combustion chamber at the sidewall of combustion chamber, the top in its gas combustion chamber is connected with exhaust opening by convection heat-exchange chamber, the bottom in gas combustion chamber is connected with the lower end, combustion chamber, described water layer wall is connected with water jacket, and its air inlet is arranged on the sidewall of body of heater.
The indoor circulating water pipe that is provided with of described heat convection, its circulating water pipe is connected with water jacket.
Described burner hearth is oval burner hearth.
The utility model has the advantages that: simple in structure, the thermal efficiency is high: adopt the reverse combustion type gas collection and burn in one, realized that the cyclic formula of fuel in combustion chamber successively burns, its thermal efficiency is up to 86.51%.Environmental protection: smoke discharge amount 0.034kg/h, sulfur dioxide concentration 0.361g/m , can't see fume emission under the normality.It is the ideal device that utilizes biomass energy.
Description of drawings
Figure is structural representation of the present utility model.
The specific embodiment
Further specify the specific embodiment of the present utility model below in conjunction with accompanying drawing.
As shown in Figure 1, biomass fuel reverse combustion type boiler of the present utility model, comprise body of heater 1, be arranged on the exhaust opening 15 on the body of heater 1, limnimeter 12, be arranged on the burner hearth 13 in the body of heater 1, the water jacket 2 that is arranged on the cooling fire grate 9 of burner hearth 13 bottoms and is arranged on burner hearth 13 peripheries, water inlet pipe 8 and outlet pipe 16, described exhaust opening 15 is connected with air-introduced machine, it is characterized in that in described burner hearth 13, being provided with water layer wall 4, described water layer wall 4 is Z-shaped structure, and burner hearth 12 is divided into top convection heat-exchange chamber 14 and lower combustion chamber 6, and in the combustion chamber 6 sidewall forms gas combustion chamber 5, the top in its gas combustion chamber 5 is connected with exhaust opening 15 by convection heat-exchange chamber 14, the bottom in gas combustion chamber 5 is connected with 6 lower ends, combustion chamber, described water layer wall 4 is connected with water jacket 2, and its air inlet 11 is arranged on the sidewall of body of heater 1.Burner hearth 13 described in the utility model is oval burner hearth.Greatly strengthen heat transfer efficiency, slowed down flue gas velocity.
Be provided with circulating water pipe 3 in the convection heat-exchange chamber 14 described in the utility model, its circulating water pipe is connected with water jacket.Effectively reduced the flue-gas temperature that exhaust opening 15 is discharged.
Operation principle of the present utility model is:
Biosolids fuel is put in the combustion chamber 6, lighted a fire at feeding mouth from fire door, the air that is blown into by air inlet 11, make the biosolids fuel combustion on 6 upper stratas, combustion chamber, on the combustion chamber, form direct burning zone 6-1, burn half broken coke fuel pre-heat effect is played by lower floor, directly the temperature of burning zone is 100 ℃～200 ℃, the excessive moisture of lower floor's biosolids fuel is dried, form drying layer 6-2, the bottom of drying layer 6-2 is destructive distillation layer 6-3, the temperature of its destructive distillation layer 6-3 is 300 ℃～400 ℃, a large amount of Volatile CH 4, H 4, the CO fuel gas, the heat of high temperature that produces by undermost oxide layer 6-4 burning enters the gas combustion chamber, and the temperature of its oxide layer 6-4 can be up to 800 ℃～and 900 ℃, mainly participate in oxidation reaction, the fuel gas of a large amount of volatilizations passes the oxide layer burning, and the oxide layer burning produces CO 2+ O 2Enter gas combustion chamber 5, reduce in gas combustion chamber 5, the circulating water pipe 3 in the hot gas of generation and the convection heat-exchange chamber 14 carries out heat exchange.Because the utility model adopts the reverse combustion type gas collection and burns in one, has realized that the cyclic formula of fuel in combustion chamber successively burns, its thermal efficiency is up to 86.51%.Environmental protection: smoke discharge amount 0.034kg/h, sulfur dioxide concentration 0.361g/m
Biomass fuel reverse combustion type boiler provided by the utility model can be used for heating, oven dry or hot water, steam etc.7 is sewage draining exit among the figure, and 10 is observation panel.
Applicable biomass solid shaping fuel (block, bar-shaped, the graininess) fuel that this implementation is novel.
Claims (3)
1. biomass fuel reverse combustion type boiler, comprise body of heater, be arranged on the exhaust opening on the body of heater, limnimeter, be arranged on the burner hearth in the body of heater, be arranged on the cooling fire grate of lower furnace portion and the water jacket that is arranged on the burner hearth periphery, water inlet pipe and outlet pipe, described exhaust opening is connected with air-introduced machine, it is characterized in that in described burner hearth, being provided with the water layer wall, described water layer wall is Z-shaped structure, and burner hearth is divided into top convection heat-exchange chamber and lower combustion chamber, and form the gas combustion chamber at the sidewall of combustion chamber, the top in its gas combustion chamber is connected with exhaust opening by convection heat-exchange chamber, the bottom in gas combustion chamber is connected with the lower end, combustion chamber, described water layer wall is connected with water jacket, and its air inlet is arranged on the sidewall of body of heater.
2. biomass fuel reverse combustion type boiler according to claim 1 is characterized in that the indoor circulating water pipe that is provided with of described heat convection, and its circulating water pipe is connected with water jacket.
3. biomass fuel reverse combustion type boiler according to claim 1 is characterized in that described burner hearth is oval burner hearth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220621176 CN202902605U (en) | 2012-11-22 | 2012-11-22 | Biomass fuel inverse combustion boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220621176 CN202902605U (en) | 2012-11-22 | 2012-11-22 | Biomass fuel inverse combustion boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202902605U true CN202902605U (en) | 2013-04-24 |
Family
ID=48123265
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220621176 CN202902605U (en) | 2012-11-22 | 2012-11-22 | Biomass fuel inverse combustion boiler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202902605U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103486564A (en) * | 2013-08-12 | 2014-01-01 | 广西天虹锅炉有限公司 | Energy-efficient steam boiler |
| CN103512191A (en) * | 2013-10-28 | 2014-01-15 | 刘备 | Segmented dynamic heat-exchange energy-saving environment-friendly boiler |
| CN103697453A (en) * | 2013-12-07 | 2014-04-02 | 唐升华 | Vapor generator |
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| CN106196004A (en) * | 2015-12-22 | 2016-12-07 | 北京林业大学 | A kind of gasified combustion apparatus |
| WO2017211130A1 (en) * | 2016-06-07 | 2017-12-14 | 广东工业大学 | Integrated system for biological particle gasification combustion and steam generation |
| CN108386830A (en) * | 2018-02-07 | 2018-08-10 | 四川省烟草公司泸州市公司 | Flue-cured tobacco biomass fuel combustion gasification all-in-one oven |
-
2012
- 2012-11-22 CN CN 201220621176 patent/CN202902605U/en not_active IP Right Cessation
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103486564A (en) * | 2013-08-12 | 2014-01-01 | 广西天虹锅炉有限公司 | Energy-efficient steam boiler |
| CN105091321A (en) * | 2013-10-28 | 2015-11-25 | 刘备 | Differential type energy-saving and environment-friendly boiler |
| CN103512191A (en) * | 2013-10-28 | 2014-01-15 | 刘备 | Segmented dynamic heat-exchange energy-saving environment-friendly boiler |
| CN105157220B (en) * | 2013-10-28 | 2017-11-21 | 张辉 | Dynamic heat-exchange energy-saving environment-protection boiler |
| CN105091321B (en) * | 2013-10-28 | 2017-10-31 | 泉州台商投资区铭源机械设备有限公司 | Differential expression energy-saving, environmental protection boiler |
| CN105091323B (en) * | 2013-10-28 | 2017-09-22 | 泉州台商投资区铭源机械设备有限公司 | Differential expression Dynamic Thermal exchanges environment-protection boiler |
| CN105157220A (en) * | 2013-10-28 | 2015-12-16 | 刘备 | Dynamic heat exchange energy-saving environment-friendly boiler |
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