CN201652308U - Biomass fuel burning device - Google Patents

Biomass fuel burning device Download PDF

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Publication number
CN201652308U
CN201652308U CN2010201625407U CN201020162540U CN201652308U CN 201652308 U CN201652308 U CN 201652308U CN 2010201625407 U CN2010201625407 U CN 2010201625407U CN 201020162540 U CN201020162540 U CN 201020162540U CN 201652308 U CN201652308 U CN 201652308U
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China
Prior art keywords
vertical shaft
shaft furnace
air
chamber
burning
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Expired - Fee Related
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CN2010201625407U
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Chinese (zh)
Inventor
杨奇飞
许金花
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GUANG DONG ZHAO FENG ENERGY TECHNOLOGY Co Ltd
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GUANG DONG ZHAO FENG ENERGY TECHNOLOGY Co Ltd
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Priority to CN2010201625407U priority Critical patent/CN201652308U/en
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Publication of CN201652308U publication Critical patent/CN201652308U/en
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Abstract

The utility model discloses a biomass fuel burning device, and provides a biomass fuel burning device with high burning efficiency and low contaminant outflow discharge. The biomass fuel burning device comprises a vertical burning furnace (1) on which a smoke removal channel (2) is arranged, the interior of the vertical burning furnace (1) comprises a burning chamber (20) and a heat exchange chamber (21), an upper grate (3) and a lower grate (4) are arranged in the burning chamber (20), a feed device communicated with the burning chamber (20) is arranged thereon on the side wall of the vertical burning furnace (1), a primary air inlet (33), a secondary air inlet (34) and a tertiary air intake device are respectively arranged on the vertical burning furnace (1) in corresponding positions, a flue gas pipe (5) and a hot water pipe (6) are arranged in the heat exchange chamber (21), and the flue gas pipe (5) is respectively communicated with the burning chamber (20) and the smoke removal channel (2). The utility model can be extensively applied in the field of boilers.

Description

Biomass fuel combustion device
Technical field
The utility model relates to a kind of biomass fuel combustion device.
Background technology
At present, common fuel generally is fossil fuels such as coal, oil, natural gas in the production, and these fossil fuels are non-renewable, shows according to statistics, and these fossil fuels will be exhausted behind a century; Simultaneously, because of fossil fuel burns in a large number, give off a large amount of carbon dioxide isothermal chamber gas, energy crisis and weather threaten, and force people to seek novel energy energetically.
Biomass granule fuel is a kind of novel energy, is mainly used in gasification and burning.2005, world's biomass solid formed fuel output surpassed 4,200,000 tons.China is as large agricultural country, and biomass resource is abundanter.According to statistics, the annual agricultural crop straw of China is produced 6.04 hundred million tons of total amounts per year, and the quantity of forest product industry wood residue is 4000 ten thousand steres; About 1 ten thousand stere of quantity of the wood residue that paper-making industry produces; The annual production of bagasse is about 4,000 ten thousand tons; The husk amount that Cereals processing factory discharges reaches 4,000 ten thousand tons every year.But annual all have a large amount of biomass resources by discarded or rotten voluntarily in vain, and the then direct burning disposal that has has not only caused the waste of resource, has also polluted environment.Therefore, it is imperative to develop this biomass granule fuel.Because the ability that stores in the living beings derives from solar energy, therefore, the burning of biomass granule fuel can not pollute environment from cycle perspective.Studies show that the sulfur content and the nitrogen content of biomass granule fuel are low, easily catch fire, the efficiency of combustion height, content of ashes is little, after the burning, SO 2And NO XAnd the discharge capacity of flue dust is more much smaller than fossil fuel, is a kind of clean energy resource.Its wide material sources, renewable, be subjected to the natural conditions restriction few.The Application and Development biomass energy develops social economy to preserving the ecological environment, and implementing the energy sustainable development strategy has major and immediate significance.
But the development of corresponding special bio matter shaped fuel combustion apparatus also seldom.Biomass molding fuel volatile matter height (generally greater than 70%), ignition temperature is low, generally separates out in a large number and takes fire at 250 ℃~350 ℃ following volatile matters, if air capacity deficiency or reaction temperature are not enough, can cracking produce a large amount of carbon blacks and tar.
Be the biological substance for combustion shaped fuel, existing biomass molding fuel combustion apparatus is improved to form on the basis of coal-burning boiler, there are un-reasonable phenomenons such as the distribution of air field of flow, fire box temperature field distribution, distribution of concentration, heating surface layout, biomass molding fuel burning normal speed and normal condition have been had a strong impact on, exhaust gas temperature surpasses 220 ℃, problems such as cause that boiler thermal output is low, black smoke billowing, slagging scorification easily, floor space are big.
The utility model content
Technical problem to be solved in the utility model is to overcome the deficiencies in the prior art, provides a kind of efficiency of combustion height, the biomass fuel combustion device that pollutant discharge amount is few.
The technical scheme that the utility model adopted is: the utility model comprises vertical shaft furnace, described vertical shaft furnace is provided with discharge flue, described vertical shaft furnace inside comprises combustion chamber and the Heat Room that air-flow communicates, described Heat Room is positioned at above the described combustion chamber and with described discharge flue air-flow and communicates, upper fire-grating and lower fire grating are set in the described combustion chamber, the sidewall that described combustion chamber is positioned at described vertical shaft furnace is provided with the pay-off that communicates with described combustion chamber, the below cloth of described lower fire grating is wind inlet once, described pay-off downside is provided with the secondary wind inlet, on the sidewall of described vertical shaft furnace and top of described upper fire-grating and the opposite that is positioned at described secondary wind inlet are provided with the tertiary air air-intake device, be provided with fume pipe in the described Heat Room and be arranged on the interior hot-water line of described fume pipe, described fume pipe communicates with described combustion chamber and described discharge flue air-flow respectively.
Described tertiary air air-intake device comprises blast pipe, the distributing wind disc of fixedlying connected with described blast pipe of fixedlying connected with described vertical shaft furnace, is arranged on the rotation blast cap on the described distributing wind disc.
Described pay-off comprises feeding screw and the hopper that is arranged on the described feeding screw, and described feeding screw communicates with described vertical shaft furnace.
Be provided with the flue gas flash chamber between described Heat Room and the described discharge flue, be provided with the eddy flow guide plate in the described flue gas flash chamber, the sidewall that described flue gas flash chamber is positioned at described vertical shaft furnace is provided with ash removing opening.
Also be provided with economizer and air preheater in the described flue gas flash chamber.
The beneficial effects of the utility model are: because the utility model vertical shaft furnace, described vertical shaft furnace is provided with discharge flue, described vertical shaft furnace inside comprises combustion chamber and the Heat Room that air-flow communicates, described Heat Room is positioned at above the described combustion chamber and with described discharge flue air-flow and communicates, upper fire-grating and lower fire grating are set in the described combustion chamber, the sidewall that described combustion chamber is positioned at described vertical shaft furnace is provided with the pay-off that communicates with described combustion chamber, the below cloth of described lower fire grating is wind inlet once, described pay-off downside is provided with the secondary wind inlet, on the sidewall of described vertical shaft furnace and top of described upper fire-grating and the opposite that is positioned at described secondary wind inlet are provided with the tertiary air air-intake device, be provided with fume pipe in the described Heat Room and be arranged on the interior hot-water line of described fume pipe, described fume pipe communicates with described combustion chamber and described discharge flue air-flow respectively, by a wind being blown into from a wind inlet, slight disturbance fuel, can avoid coking, promote fuel completing combustion, secondary wind is blown into from the brute force of secondary wind inlet, flame is burnt to the other end, then under the effect of the spiral tertiary air that is positioned at described upper fire-grating top, combustion product is tightly pinned by wind-force, carry out abundant mixed combustion, so the utility model biomass molding fuel efficiency of combustion height, pollutant discharge amount is few.
Owing to be provided with the flue gas flash chamber between described Heat Room and the described discharge flue; be provided with the eddy flow guide plate in the described flue gas flash chamber; the sidewall that described flue gas flash chamber is positioned at described vertical shaft furnace is provided with ash removing opening; the cigarette ash of discharging from described hot cell is during through described flue gas flash chamber; under the effect of eddy flow guide plate; dust in the flue gas deposits at this; get rid of by described ash removing opening then; avoid dust directly to be discharged into contaminated air in the air, so the utility model is of value to environmental protection.
Owing to be provided with economizer and air preheater in the described flue gas flash chamber, absorb the heat of low-temperature flue gas by described economizer, reduce exhaust gas temperature, reduce flue gas loss, fuel saving adopts high-temperature air burning by described air preheater, improves burning condition, the heat loss due to incomplete combustion of fuel is descended, thereby can further improve boiler thermal output; In addition, after the burning of employing hot-air, temperature raises in the stove, and radiant heat transfer is strengthened, and can save evaporating heating surface, so the utility model cost is low, result of use is good, and boiler thermal output is low, and floor space is little.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The specific embodiment
As shown in Figure 1, the utility model comprises vertical shaft furnace 1, described vertical shaft furnace 1 top is provided with discharge flue 2, described vertical shaft furnace 1 inside comprises combustion chamber 20, Heat Room 21, the flue gas flash chamber 22 that air-flow communicates, be provided with upper fire-grating 3, lower fire grating 4 and tertiary air air-intake device in the described combustion chamber 20, described upper fire-grating 3, described lower fire grating 4 all adopt the membrane type structure, have both increased heat transfer area and have also improved the coefficient of conductivity, and the heat transfer rate is fast.Therefore the boiler hearth temperature field distribution is even, thermal efficiency height, be provided with pay-off on the sidewall of described vertical shaft furnace 1 and between described upper fire-grating 3 and described lower fire grating 4, described pay-off comprises feeding screw 31 and is arranged on hopper 32 on the described feeding screw 31, described feeding screw 31 passes described vertical shaft furnace 1 and communicates with its inside, the sidewall on described pay-off opposite is provided with observation window 11, described lower fire grating 4 is downward-sloping gradually from described pay-off end to end, and be divided into laydown area successively, the solid phase combustion zone, the gas-phase combustion district, described laydown area is away from a side-lower cloth of described pay-off wind inlet 33 once, one time wind passes through slightly disturbance fuel of a described wind inlet 33, fuel is stirred to avoid coking, promote the completing combustion of fuel, described pay-off lower end is provided with secondary wind inlet 34, secondary wind is from described secondary wind inlet 34 powerful being blown into, fuel and flame are burnt to described gas-phase combustion district, on the sidewall of described vertical shaft furnace 1 and top of described upper fire-grating 4 and the opposite that is positioned at described secondary wind inlet 34 are provided with the tertiary air air-intake device, described tertiary air air-intake device comprises blast pipe 13, distributing wind disc 14 and rotation blast cap 15, described blast pipe 13 is fixedly installed on the described vertical shaft furnace 1, described blast pipe 13 is a bend pipe, described blast pipe 13 1 ends pass described vertical shaft furnace 1 and communicate with the external world, the other end communicates with described distributing wind disc 14, described rotation blast cap 15 is arranged on the described distributing wind disc 14, blow out spiral tertiary air and the comprehensive function of secondary wind through described rotation blast cap 15, the solid phase combustion product is tightly pinned and constantly mixed combustion in described gas-phase combustion district, be provided with Heat Room 21 above the described combustion chamber 20, described Heat Room 21 comprises fume pipe 5 and passes the hot-water line 6 of described fume pipe 5, described hot-water line 6 is the membrane type water pipe, described fume pipe 5 one ends communicate with described combustion chamber 20, the other end communicates with described flue gas flash chamber 22, described flue gas flash chamber 22 communicates with described discharge flue 2, be provided with eddy flow guide plate 7 in the described flue gas flash chamber 22, economizer 8 and air preheater 9, the sidewall that described flue gas flash chamber 22 is positioned at described vertical shaft furnace 1 is provided with ash removing opening 10, flue gas is through after described hot-water line 6 heat exchange, pass through described economizer 8 and described air preheater 9 again, flue gas flow rate reduces, under the effect of described eddy flow guide plate 7, dust in the flue gas deposits at this, get rid of by described ash removing opening 10 then, avoid directly being discharged into contaminated air in the air.
The utility model can be widely used in field of boilers.

Claims (5)

1. biomass fuel combustion device, it comprises vertical shaft furnace (1), described vertical shaft furnace (1) is provided with discharge flue (2), it is characterized in that: described vertical shaft furnace (1) inside comprises combustion chamber (20) and the Heat Room (21) that air-flow communicates, described Heat Room (21) is positioned at above the described combustion chamber (20) and with described discharge flue (2) air-flow and communicates, upper fire-grating (3) and lower fire grating (4) are set in the described combustion chamber (20), the sidewall that described combustion chamber (20) is positioned at described vertical shaft furnace (1) is provided with the pay-off that communicates with it, the below cloth of described lower fire grating (3) is wind inlet (33) once, described pay-off downside is provided with secondary wind inlet (34), on the sidewall of described vertical shaft furnace (1) and top of described upper fire-grating (4) and the opposite that is positioned at described secondary wind inlet (34) are provided with the tertiary air air-intake device, be provided with fume pipe (5) in the described Heat Room (21) and be arranged on the interior hot-water line (6) of described fume pipe (5), described fume pipe (5) communicates with described combustion chamber (20) and described discharge flue (2) air-flow respectively.
2. biomass fuel combustion device according to claim 1 is characterized in that: described tertiary air air-intake device comprises blast pipe (13), the distributing wind disc (14) of fixedlying connected with described blast pipe (13) of fixedlying connected with described vertical shaft furnace (1), is arranged on the rotation blast cap (15) on the described distributing wind disc (14).
3. biomass molding fuel burner according to claim 1, it is characterized in that: described pay-off comprises feeding screw (31) and is arranged on hopper (32) on the described feeding screw (31) that described feeding screw (31) communicates with described vertical shaft furnace (1).
4. according to each described biomass fuel combustion device of claim 1 to 3, it is characterized in that: be provided with flue gas flash chamber (22) between described Heat Room (21) and the described discharge flue (2), be provided with eddy flow guide plate (7) in the described flue gas flash chamber (22), the sidewall that described flue gas flash chamber (22) is positioned at described vertical shaft furnace (1) is provided with ash removing opening (10).
5. biomass fuel combustion device according to claim 4 is characterized in that: also be provided with economizer (8) and air preheater (9) in the described flue gas flash chamber (22).
CN2010201625407U 2010-04-13 2010-04-13 Biomass fuel burning device Expired - Fee Related CN201652308U (en)

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CN2010201625407U CN201652308U (en) 2010-04-13 2010-04-13 Biomass fuel burning device

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Application Number Priority Date Filing Date Title
CN2010201625407U CN201652308U (en) 2010-04-13 2010-04-13 Biomass fuel burning device

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104075314A (en) * 2014-07-18 2014-10-01 临沭县东方红锅炉制造有限公司 Biomass particle suspension combustion boiler
CN104089280A (en) * 2014-07-18 2014-10-08 临沭县东方红锅炉制造有限公司 Boiler biomass particle combustion device
CN104913497A (en) * 2014-03-14 2015-09-16 佛山市顺德区旭政实业有限公司 Biomass particle heating water heater
CN105465760A (en) * 2015-12-24 2016-04-06 浙江锅炉有限公司 Biomass steam generator
CN112833383A (en) * 2021-01-06 2021-05-25 刘传祥 Vertical biomass briquetting solid fuel boiler
CN113606778A (en) * 2021-07-23 2021-11-05 李志旭 Energy-saving boiler
CN116557948A (en) * 2023-06-05 2023-08-08 青海万佳禾环保科技有限公司 Pasture heating stove control system and control method thereof

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104913497A (en) * 2014-03-14 2015-09-16 佛山市顺德区旭政实业有限公司 Biomass particle heating water heater
CN104075314A (en) * 2014-07-18 2014-10-01 临沭县东方红锅炉制造有限公司 Biomass particle suspension combustion boiler
CN104089280A (en) * 2014-07-18 2014-10-08 临沭县东方红锅炉制造有限公司 Boiler biomass particle combustion device
CN105465760A (en) * 2015-12-24 2016-04-06 浙江锅炉有限公司 Biomass steam generator
CN105465760B (en) * 2015-12-24 2018-12-04 浙江锅炉有限公司 A kind of biomass steam generator
CN112833383A (en) * 2021-01-06 2021-05-25 刘传祥 Vertical biomass briquetting solid fuel boiler
CN113606778A (en) * 2021-07-23 2021-11-05 李志旭 Energy-saving boiler
CN113606778B (en) * 2021-07-23 2022-09-20 中粮屯河伊犁新宁糖业有限公司 Energy-saving boiler
CN116557948A (en) * 2023-06-05 2023-08-08 青海万佳禾环保科技有限公司 Pasture heating stove control system and control method thereof

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20101124

Termination date: 20150413

EXPY Termination of patent right or utility model