CN107101219A - A kind of circulation air path device of biomass boiler - Google Patents
A kind of circulation air path device of biomass boiler Download PDFInfo
- Publication number
- CN107101219A CN107101219A CN201710240049.8A CN201710240049A CN107101219A CN 107101219 A CN107101219 A CN 107101219A CN 201710240049 A CN201710240049 A CN 201710240049A CN 107101219 A CN107101219 A CN 107101219A
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- CN
- China
- Prior art keywords
- vault
- air
- biomass boiler
- path device
- pipeline
- 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.)
- Pending
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K1/00—Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
- F23K1/04—Heating fuel prior to delivery to combustion apparatus
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/02—Pneumatic feeding arrangements, i.e. by air blast
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Air Supply (AREA)
- Solid-Fuel Combustion (AREA)
Abstract
The present invention relates to a kind of biomass boiler system, more particularly, to a kind of circulation air path device of biomass boiler.A kind of circulation air path device of biomass boiler, including body of heater, combustion chamber, mobile grate, charging gear and drum, also include the first inlet air plenum, the second inlet air plenum being arranged on below the discharging opening of charging gear and the exhaust opening being arranged on combustion chamber, exhaust opening is connected with flue, the other end of flue is connected on the entrance of deduster, the outlet of deduster is connected to charging gear by pipeline and material is dried, flue is provided with the air preheater to air preheat using the flue gas in pipeline, the entrance of air preheater is connected with the first air blower, its outlet is connected by pipeline with the first inlet air plenum, second inlet air plenum is connected by pipeline with the second air blower.The present invention is simple in construction, effective to improve the utilization rate of the energy, while having preferable dust removing effects, realizes recycling and reusing for energy, reduces cost.
Description
Technical field
The present invention relates to a kind of biomass boiler system, more particularly, to a kind of circulation air path device of biomass boiler.
Background technology
With the development of society, the mankind are more and more to the demand of the energy, and the reserves such as conventional energy resource coal, oil have
Limit, and these energy can cause various environmental problems during use.Therefore, people start development it is renewable, pollution-free
Biomass energy, matched is exactly biomass boiler.At present, the biomass boiler thermal efficiency only has 80% or so, energy profit
Low with rate, while the exhaust gas temperature of existing biomass boiler is general at 180 DEG C~150 DEG C, this partial fume energy can account for pot
The 7~9% of stove fuel gross energy, this partial fume heat energy is discharged in an atmosphere, the significant wastage of the energy is caused, also to surrounding
Environment causes thermal pollution.
The content of the invention
For above-mentioned produced problem, it is an object of the invention to provide a kind of circulation air path device of biomass boiler,
The apparatus structure is simple, the effective utilization rate for improving the energy, while having preferable dust removing effects, realizes the recovery weight of energy
It is multiple to utilize, reduce cost.
To reach above-mentioned purpose, technical scheme is as follows:
A kind of circulation air path device of biomass boiler, including body of heater, be arranged on the combustion chamber of the furnace interior, be arranged on institute
State the mobile grate of bottom of combustion chamber, the charging gear being arranged at the mobile grate and be arranged on above the combustion chamber
Drum, in addition to be arranged on the first inlet air plenum below the mobile grate, be arranged under the discharging opening of the charging gear
Second inlet air plenum of side and the exhaust opening being arranged on the combustion chamber, the exhaust opening are connected with flue, the cigarette
The other end of feed channel is connected on the entrance of deduster, and the outlet of deduster is connected to charging gear by pipeline and material is entered
Row drying, the flue is provided with using the flue gas in pipeline to the air preheater of air preheat, the air preheat
The entrance of device is connected with the first air blower, and its outlet is connected by pipeline with first inlet air plenum, second inlet air plenum
It is connected by pipeline with second air blower.
In the above-mentioned technical solutions, of the invention simple in construction, air is delivered to air preheater by the first air blower,
Carry out heating up after heat exchange by the higher waste gas of air preheater and temperature, the hot-air after preheating is entered by the first inlet air plenum
Enter in burner hearth, material is entered in body of heater by charging gear, the second air blower blasts air from the second inlet plenum, air will
Material is dispelled so that material arrangement is uniform, and after material is burnt, waste gas is arranged by the exhaust opening of combustion chamber through exhaust gases passes
Go out, hot flue gas carries out that heat exchange is laggard to cross deduster dust removal by filtration with air preheater, and the air after dedusting is in flow direction feed dress
Put it is interior material is dried, therefore formed circulation wind path so that energy regenerating reuse, burn it is more abundant, more save
Environmental protection.
As the preferred of above-mentioned technical proposal, second inlet plenum is located at the top of the mobile grate.
As the preferred of above-mentioned technical proposal, the rear end of the mobile grate is provided with the first vault, the second vault and the
Three vaults, the height of first vault is higher than the second vault, and the height of second vault is higher than the 3rd vault.
As the preferred of above-mentioned technical proposal, the distance between the bottom of the 3rd vault and the top of mobile grate are
In 0-10 centimeters.
As the preferred of above-mentioned technical proposal, formed between first vault and second vault and the 3rd vault
Stepped vault.Dust certain in flue gas can be blocked, effectively by the high-temperature flue gas stream and mistake of fire grate rear end superjacent air space
Measure air and be oriented to combustion centre so that burning is more concentrated.
As the preferred of above-mentioned technical proposal, the body of heater, the first vault, the second vault and the 3rd vault are by refractory brick
It is built into.
As the preferred of above-mentioned technical proposal, polylith flow apron is provided with the deduster, the flow apron will be removed
Dirt device is divided into multiple expansion chambers.The expansion chamber that waste gas is flowed through gradually increases, and because flow velocity declines, dust gravitational settling is collected, water conservancy diversion
Baffle plate extends holdup time of the waste gas in expansion chamber, strengthens dust removal effect.
As the preferred of above-mentioned technical proposal, the flow apron dislocation is disposed with three pieces.
The invention has the advantages that:
1st, contact drying is carried out simultaneously using the exhaust fumes produced in biomass boiler production process as load using heat exchange
There is provided energy utilization rate for gas convection drying.
2nd, fume afterheat first carries out heat exchange, preheated air, then drying object by cascade utilization by air preheater and air
Material, has the advantages that high-efficient energy-saving environment friendly.
3rd, biomass material drying, combustion integrative, realize high water content biomass material and directly use, reduce and build
If land used, cost of investment is reduced.
4th, the deduster that the system is used, reaches dust removing effects, eliminates the conventional dust removal system such as bag-type dust, equipment is more
Simply, maintenance operation cost is relatively low.
Brief description of the drawings
Fig. 1 is overall structure diagram of the invention;
Fig. 2 is A portions enlarged diagram in figure.
Embodiment
Technical scheme will be clearly and completely described below, it is clear that described embodiment is only
A part of embodiment of the present invention, rather than whole embodiments.Embodiment in the present invention, those of ordinary skill in the art are not having
There is all other embodiment done and obtained under the premise of creative work, belong to the scope of protection of the invention.
With embodiment, the present invention is described in detail below in conjunction with the accompanying drawings.
Embodiment 1:With reference to Fig. 1 and Fig. 2, a kind of circulation air path device of biomass boiler, including body of heater 7, it is arranged on stove
The internal combustion chamber 8 of body 7, the mobile grate 9 for being arranged on the bottom of combustion chamber 8, the charging gear 11 being arranged at mobile grate 9, set
Put the drum 10 above combustion chamber 8, the first inlet air plenum 12 being arranged on below mobile grate 9, be arranged on charging gear 11
The second inlet air plenum 13 between discharging opening and mobile grate and the exhaust opening 14 being arranged on combustion chamber 8, exhaust opening 14 are connected
There is flue 15, the other end of flue 15 is connected on the entrance of deduster 16, and the outlet of deduster 16 passes through pipeline
It is connected to charging gear 11 to dry material, flue 15 is provided with the sky to air preheat using the flue gas in pipeline
Air preheater 17, the entrance of air preheater 17 is connected with the first air blower 18, and it, which is exported, passes through pipeline and the first inlet air plenum 12
It is connected, the second inlet air plenum 13 is connected by pipeline with the second air blower 19.
With reference to Fig. 1 and Fig. 2, the rear end of mobile grate 9 is provided with the first vault 71, the second vault 72 and the 3rd vault 73,
The height of first vault 71 is higher than the second vault 72, and the height of the second vault 72 is higher than the 3rd vault 73, the bottom of the 3rd vault 73
The distance between portion and the top of mobile grate 9 are interior for 0-10 centimeters, the first vault 71 and the second vault 72 and the 3rd vault
Stepped vault is formed between 73.Dust certain in flue gas can be blocked, effectively by the high temperature of fire grate rear end superjacent air space
Flue gas stream and excess air are oriented to combustion centre so that burning is more concentrated.
With reference to Fig. 1 and Fig. 2, body of heater 7, the first vault 71, the second vault 72 and the 3rd vault 73 are built into by refractory brick.
With reference to Fig. 1 and Fig. 2, polylith flow apron 161 is provided with deduster 16, deduster 16 is divided into by flow apron 161
Multiple expansion chambers 162, the dislocation of flow apron 161 is disposed with three pieces.The expansion chamber 162 that waste gas is flowed through gradually increases, because under flow velocity
Drop, dust gravitational settling is collected, and flow apron 161 extends holdup time of the waste gas in expansion chamber 162, is strengthened dust and is removed
Effect.
The present invention's is simple in construction, and during work, air is delivered to air preheater 17 by the first air blower 18, passes through sky
Air preheater 17 is carried out heating up after heat exchange with the higher waste gas of temperature, and the hot-air after preheating is entered by the first inlet air plenum 12
In burner hearth, material is entered in body of heater 7 by charging gear 11, and the second air blower 19 blasts air from the second inlet plenum, empty
Gas dispels material so that material arrangement is uniform, and after material is burnt, waste gas is by the exhaust opening 14 of combustion chamber 8 through flue gas
Passage is discharged, and hot flue gas carries out that heat exchange is laggard to cross the dust removal by filtration of deduster 16 with air preheater 17, and the air after dedusting exists
Flow to and material is dried in charging gear 11, therefore form circulation wind path so that energy regenerating is reused, and burning is more filled
Point, more energy-conserving and environment-protective.
The better embodiment to this patent is explained in detail above, but this patent is not limited to above-mentioned embodiment party
, can also be on the premise of this patent objective not be departed from formula, the knowledge that one skilled in the relevant art possesses
Various changes can be made.
Claims (8)
1. a kind of circulation air path device of biomass boiler, including body of heater(7), be arranged on the body of heater(7)Internal combustion chamber
(8), be arranged on the combustion chamber(8)The mobile grate of bottom(9), be arranged on the mobile grate(9)The charging gear at place
(11)And it is arranged on the combustion chamber(8)The drum of top(10), it is characterised in that:Also include being arranged on the mobile grate
(9)First inlet air plenum of lower section(12), be arranged on the charging gear(11)Discharging opening below the second inlet air plenum(13)With
And it is arranged on the combustion chamber(8)On exhaust opening(14), the exhaust opening(14)It is connected with flue(15), the flue gas
Pipeline(15)The other end be connected to deduster(16)Entrance on, deduster(16)Outlet by pipeline be connected to feed dress
Put(11)Material is dried, the flue(15)It is provided with pre- to the air of air preheat using the flue gas in pipeline
Hot device(17), the air preheater(17)Entrance and the first air blower(18)It is connected, it is exported by pipeline and described the
One inlet air plenum(12)It is connected, second inlet air plenum(13)Pass through pipeline and second air blower(19)It is connected.
2. a kind of circulation air path device of biomass boiler according to claim 1, it is characterised in that:Second air intake
Room(13)Positioned at the mobile grate(9)Top.
3. a kind of circulation air path device of biomass boiler according to claim 1, it is characterised in that:The mobile grate
(9)Rear end be provided with the first vault(71), the second vault(72)And the 3rd vault(73), first vault(71)Height
Higher than the second vault(72), second vault(72)Height be higher than the 3rd vault(73).
4. a kind of circulation air path device of biomass boiler according to claim 3, it is characterised in that:3rd vault
(73)Bottom and mobile grate(9)The distance between top it is interior for 0-10 centimeter.
5. a kind of circulation air path device of biomass boiler according to claim 3, it is characterised in that:First vault
(71)With second vault(72)And the 3rd vault(73)Between form stepped vault.
6. a kind of circulation air path device of biomass boiler according to claim 1, it is characterised in that:The body of heater(7)、
First vault(71), the second vault(72)And the 3rd vault(73)It is built into by refractory brick.
7. a kind of circulation air path device of biomass boiler according to claim 1, it is characterised in that:The deduster
(16)It is interior to be provided with polylith flow apron(161), the flow apron(161)By deduster(16)It is divided into multiple expansion chambers(162).
8. a kind of circulation air path device of biomass boiler according to claim 7, it is characterised in that:The flow apron
(161)Dislocation is disposed with three pieces.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710240049.8A CN107101219A (en) | 2017-04-13 | 2017-04-13 | A kind of circulation air path device of biomass boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710240049.8A CN107101219A (en) | 2017-04-13 | 2017-04-13 | A kind of circulation air path device of biomass boiler |
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Publication Number | Publication Date |
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CN107101219A true CN107101219A (en) | 2017-08-29 |
Family
ID=59675017
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201710240049.8A Pending CN107101219A (en) | 2017-04-13 | 2017-04-13 | A kind of circulation air path device of biomass boiler |
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CN (1) | CN107101219A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108326009A (en) * | 2018-02-01 | 2018-07-27 | 上海盛弘环境科技有限公司 | A kind of rubbish is converted into the processing system of distributed energy |
CN108911473A (en) * | 2018-08-30 | 2018-11-30 | 东莞市金茂污泥处置有限公司 | Direct heating type sludge drying charing mechanism |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2907198A1 (en) * | 2006-10-12 | 2008-04-18 | S N E Ronot | BURNER WITH CEREALS |
CN101975388A (en) * | 2010-10-15 | 2011-02-16 | 华南理工大学 | Biomass boiler system capable of saving energy and reducing emission |
EP2458274A1 (en) * | 2010-11-29 | 2012-05-30 | Linka Maskinfabrik A/S | Particulate solid fuel burner with special overfire air injection |
CN203784932U (en) * | 2014-03-20 | 2014-08-20 | 浙江中吉新能源有限公司 | Biomass boiler |
CN106369591A (en) * | 2016-08-25 | 2017-02-01 | 海伦市利民节能锅炉制造有限公司 | Biomass boiler for boiler front flue gas drying and continuous bale combustion |
-
2017
- 2017-04-13 CN CN201710240049.8A patent/CN107101219A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2907198A1 (en) * | 2006-10-12 | 2008-04-18 | S N E Ronot | BURNER WITH CEREALS |
CN101975388A (en) * | 2010-10-15 | 2011-02-16 | 华南理工大学 | Biomass boiler system capable of saving energy and reducing emission |
EP2458274A1 (en) * | 2010-11-29 | 2012-05-30 | Linka Maskinfabrik A/S | Particulate solid fuel burner with special overfire air injection |
CN203784932U (en) * | 2014-03-20 | 2014-08-20 | 浙江中吉新能源有限公司 | Biomass boiler |
CN106369591A (en) * | 2016-08-25 | 2017-02-01 | 海伦市利民节能锅炉制造有限公司 | Biomass boiler for boiler front flue gas drying and continuous bale combustion |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108326009A (en) * | 2018-02-01 | 2018-07-27 | 上海盛弘环境科技有限公司 | A kind of rubbish is converted into the processing system of distributed energy |
CN108911473A (en) * | 2018-08-30 | 2018-11-30 | 东莞市金茂污泥处置有限公司 | Direct heating type sludge drying charing mechanism |
CN108911473B (en) * | 2018-08-30 | 2023-10-24 | 金茂(深圳)生态科技有限公司 | Direct heating type sludge drying and carbonizing mechanism |
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PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
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Application publication date: 20170829 |