CN204756893U - Interior burning formula biomass boiler - Google Patents
Interior burning formula biomass boiler Download PDFInfo
- Publication number
- CN204756893U CN204756893U CN201520457011.2U CN201520457011U CN204756893U CN 204756893 U CN204756893 U CN 204756893U CN 201520457011 U CN201520457011 U CN 201520457011U CN 204756893 U CN204756893 U CN 204756893U
- Authority
- CN
- China
- Prior art keywords
- smoke box
- combustion chamber
- flue
- heater
- communicated
- 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 20
- 239000000779 smoke Substances 0.000 claims abstract description 80
- 238000002485 combustion reaction Methods 0.000 claims abstract description 60
- 239000002893 slag Substances 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000009826 distribution Methods 0.000 claims abstract description 9
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 12
- 239000003546 flue gas Substances 0.000 claims description 12
- 239000000428 dust Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 5
- 238000005266 casting Methods 0.000 claims description 3
- 239000000446 fuel Substances 0.000 abstract description 23
- 230000005855 radiation Effects 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 235000017060 Arachis glabrata Nutrition 0.000 description 1
- 244000105624 Arachis hypogaea Species 0.000 description 1
- 235000010777 Arachis hypogaea Nutrition 0.000 description 1
- 235000018262 Arachis monticola Nutrition 0.000 description 1
- 235000016068 Berberis vulgaris Nutrition 0.000 description 1
- 241000335053 Beta vulgaris Species 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 241000353135 Psenopsis anomala Species 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 235000020232 peanut Nutrition 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Solid-Fuel Combustion (AREA)
Abstract
The utility model provides an interior burning formula biomass boiler, relates to biomass fuel combustion apparatus technical field. The furnace body divide into that the heat production of mutual intercommunication is regional, the heat transfer is regional, in the heat production region feed arrangement the discharge gate with set up in the feed inlet of combustion chamber lateral wall intercommunication, the slag is collected the room and is located the combustion chamber below, furnace locates the combustion chamber top, the combustion chamber is collected with the slag and is equipped with the grate between the room, collects upward slag notch of smelter body outer wall that the room corresponds with the slag, is equipped with the air distribution equipment of symmetric distribution on the lateral wall of combustion chamber, the below is equipped with some firearms, in the heat transfer region upper portion, the lower part of furnace body be equipped with respectively with water inlet, the delivery port of the outside intercommunication of furnace body, go up the smoke box with down through flue tied in a bundle intercommunication between the smoke box, go up the smoke box, down smoke box, flue tied in a bundle and form the water jacket between the furnace body, go up smoke box and furnace intercommunication, lower smoke box and draught fan intercommunication. After adopting above -mentioned structure, the compact structure of boiler increases radiation heat transfer efficiency.
Description
Technical field
The utility model relates to biomass fuel combustion equipment technical field.
Background technology
Biomass energy particle fuel is a great scientific achievement in burn application.It is the crops utilizing stalk, paddy rice stalk, yule logs, wood chip, peanut shell, melon seed cases, beet pulp and bark etc. discarded, through techniques such as pulverizing-mixing-extruding-oven dry, make granular fuel, widely distributed by its raw material, the advantage of processing technology advanced person, biomass energy particle material is famous with green coal.Biomass boiler also arises at the historic moment subsequently.
And the combustion chamber of a lot of biomass boiler is arranged at the outside of body of heater at present, not only takes up room large, in heat conduction process, also easily cause the loss of heat, reduce the heat production efficiency of boiler.
Utility model content
The technical problems to be solved in the utility model is for above-mentioned the deficiencies in the prior art, provides a kind of combustion formula biomass boiler, compact conformation, increases fix density of radiate heat exchange, reaches the effect of fuel vapor.
For solving the problems of the technologies described above, technical solution adopted in the utility model is:
A kind of combustion formula biomass boiler, comprises body of heater, described body of heater be divided into be interconnected heat producing regions, heat exchange area;
Described heat producing regions comprises feed arrangement, combustion chamber, slag collection room, burner hearth, the discharging opening of described feed arrangement is communicated with the charging aperture being arranged at described sidewall of combustion chamber, described slag collection room is located at below described combustion chamber, described burner hearth is located at above described combustion chamber, fire grate is provided with between described combustion chamber and described slag collection room, the furnace body outer wall corresponding with described slag collection room is provided with slag notch, described sidewall of combustion chamber is provided with symmetrical air distribution device, and below is provided with igniter;
Described heat exchange area comprises the upper smoke box being located at top, described heat exchange area, the lower smoke box being located at bottom, described heat exchange area, the top of the body of heater corresponding with described heat exchange area, bottom are respectively equipped with and the water inlet of body of heater ft connection, delivery port, be communicated with by boundling flue between described upper smoke box with described lower smoke box, described upper smoke box, lower smoke box, between boundling flue and described body of heater, form water jacket, described upper smoke box is communicated with by flue with described burner hearth, and described lower smoke box is communicated with the air-introduced machine being located at body of heater outside by flue.
As further technical scheme, described upper smoke box comprises the first upper smoke box, the second upper smoke box that set gradually, described lower smoke box comprises the first lower smoke box, the second lower smoke box that set gradually, described first upper smoke box is communicated with described burner hearth, described second lower smoke box is communicated with described air-introduced machine, all be communicated with by boundling flue between described first upper smoke box with described first lower smoke box, between described first lower smoke box with described second upper smoke box and between described second upper smoke box with described second lower smoke box, make flue gas tortuous advance in described heat exchange area.
As further technical scheme, the air outlet of described air-introduced machine is connected with dust arrester.
As further technical scheme, described fire grate is casting furnace grate.
As further technical scheme, the charging aperture place of described combustion chamber is provided with rotary blade.
As further technical scheme, the furnace body outer wall corresponding with described combustion chamber is provided with can the finder of switch.
As further technical scheme, described feed arrangement is auger type feed arrangement.
The beneficial effect adopting technique scheme to produce is:
Adopt the structure that combustion chamber is built-in, make the compact conformation of boiler, floor space is little, not only the thermal loss of flue gas in conductive process can be reduced, the waste heat that combustion chamber can also be distributed in combustion is farthest kept in body of heater, increases radiation heat transfer efficiency.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1, body of heater; 2, heat producing regions; 20, feed arrangement; 21, combustion chamber; 22, slag collection room; 23, burner hearth; 24, fire grate; 26, slag notch; 27, igniter; 28, air distribution device; 3, heat exchange area; 31, water jacket; 32, upper smoke box; 321, the first upper smoke box; 322, the second upper smoke box; 33, lower smoke box; 331, the first lower smoke box; 332, the second lower smoke box; 34, delivery port; 35, water inlet; 36, boundling flue; 4, air-introduced machine; 5, dust arrester; 6, finder.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
As shown in Figure 1, be an embodiment of a kind of combustion formula of the utility model biomass boiler, comprise:
Body of heater 1, body of heater be divided into be interconnected heat producing regions 2, heat exchange area 3.Heat producing regions 2, for firing biomass fuel, produces heat; Heat exchange area 3, for the heat of flue gas and water are carried out heat exchange, reaches the object of heating.
Heat producing regions 2 comprises feed arrangement 20, combustion chamber 21, slag collection room 22, burner hearth 23.Feed arrangement 20 is auger type feed arrangement, by auger by fuel area density to discharging opening, reach the object of the inlet amount accurately controlling fuel, its discharging opening is communicated with the charging aperture being arranged at combustion chamber 21 sidewall.Slag collection room 22 is located at below combustion chamber 21, fire grate 24 is provided with between combustion chamber 21 and slag collection room 22, fire grate 24 is casting furnace grate, slag notch 26 on body of heater 1 outer wall corresponding with slag collection room 22, when the fuel afterburnt, it is inner that ashes can drop to slag collection room 22, cleaning by opening slag notch 26 pairs of boilers, easy and simple to handle.And fire grate 24 good heat resistance of cast iron, use cost performance very high in the boiler.
Burner hearth 23 is located at above combustion chamber 21, and the while that fuel being internally fired in combustion chamber 21, flame and flue gas are gushed out along with air-flow in burner hearth 23, the heat of release burning.Combustion chamber 21 sidewall is provided with symmetrical air distribution device 28, is provided with igniter 27 in the below of fire grate 24, the ignited fuel of igniter 27 for suspending, and the thermal current that fuel combustion produces also is that fuel can keep one of factor suspended.Because the gas flowing in stove is caused by the air-flow acting in conjunction manufacturing negative pressure and burning generation in stove of bleeding of air-introduced machine 4, therefore, the air distribution device 28 communicated with outside air carries out the supply of gas, makes pressure in stove be unlikely to too low, the oxygen simultaneously needed for aftercombustion; Because air distribution device 28 is oppositely arranged, can eddy current be formed in combustion chamber 21, keep the suspended state of fuel in combustion chamber 21, make burning more abundant.
The charging aperture place of combustion chamber 21 is provided with rotary blade, if there is part powder fuel to lump in feed arrangement 20, then directly can affects combustion efficiency, therefore add rotary blade at charging aperture place, the fuel of this caking can be smashed, improve efficiency of combustion further.The furnace body outer wall corresponding with combustion chamber 21 is provided with can the finder 6 of switch, and can observe the combustion case of fuel at any time, handled easily personnel make debugging to combustion process.
Heat exchange area 3 comprises the upper smoke box 32 being located at top, heat exchange area 3, the lower smoke box 33 being located at heat exchange area 3, the top of the body of heater corresponding with heat exchange area 3, bottom are respectively equipped with and the water inlet 35 of body of heater ft connection, delivery port 34, be communicated with by boundling flue 36 between upper smoke box 32 with lower smoke box 33, upper smoke box 32, lower smoke box 33, between boundling flue 36 and described body of heater, form water jacket 31, upper smoke box 32 is communicated with by flue with burner hearth 23, and lower smoke box 33 is communicated with the air-introduced machine 4 being located at body of heater outside by flue.Upper smoke box comprises the first upper smoke box 321, second upper smoke box 322 set gradually, lower smoke box comprises the first lower smoke box 331, second lower smoke box 332 set gradually, first upper smoke box 321 is communicated with by flue with burner hearth 23, and the second lower smoke box 332 is communicated with the air-introduced machine 4 being located at body of heater outside by flue.All be communicated with by boundling flue 36 between first upper smoke box 321 with the first lower smoke box 331, between the first lower smoke box 331 with the second upper smoke box 322 and between the second upper smoke box 322 with the second lower smoke box 332, make flue gas tortuous advance in described heat exchange area.This design adds the formation of flue gas in the body of road, too increases the contact area between pipeline and water, and then adds the efficiency of radiation heat transfer.
The air outlet of air-introduced machine 4 is connected with dust arrester 5.Owing to there is dust granules in flue gas, directly flue gas to environment, can pass into after cleaner purifies and discharges, can effectively reduce pollution level by discharge.
Use procedure:
First water is introduced in water jacket 31 by water inlet 35.Fuel is put into feed arrangement 20, auger is by the feeding discharging opening of quota of fuel.Fuel is through the charging aperture of combustion chamber 21, and period is rubbed again by rotary blade.Igniter 27 is by ignited fuel, and air distribution device 28 is also quantitative under the effect of negative pressure sends air into combustion chamber 21, keeps the suspended state of fuel.With igniter 27 pilot fuel, open air-introduced machine 4 subsequently and bleed, cause negative pressure state in stove.The flame that burning produces and flue gas enter burner hearth 23, then enter upper smoke box 32, boundling flue 36, lower smoke box 33 successively along with air-flow, and period carries out radiation heat transfer with peripheral water, and complete the heating to water, the water after heating is discharged from delivery port 34.Remaining flue gas is discharged along with air-introduced machine 4, then is discharged in air through the purification of dust arrester 5.
Adopt the structure that combustion chamber is built-in, make the compact conformation of boiler, floor space is little, not only the thermal loss of flue gas in conductive process can be reduced, the waste heat that combustion chamber can also be distributed in combustion is farthest kept in body of heater, increases radiation heat transfer efficiency.
Claims (7)
1. a combustion formula biomass boiler, is characterized in that: comprise body of heater (1), described body of heater (1) be divided into be interconnected heat producing regions (2), heat exchange area (3);
Described heat producing regions (2) comprises feed arrangement (20), combustion chamber (21), slag collection room (22), burner hearth (23), the discharging opening of described feed arrangement (20) is communicated with the charging aperture being arranged at described combustion chamber (21) sidewall, described slag collection room (22) is located at below, described combustion chamber (21), described burner hearth (23) is located at top, described combustion chamber (21), fire grate (24) is provided with between described combustion chamber (21) and described slag collection room (22), body of heater (1) outer wall corresponding with described slag collection room (22) is provided with slag notch (26), described combustion chamber (21) sidewall is provided with symmetrical air distribution device (28), below is provided with igniter (27),
Described heat exchange area (3) comprises the upper smoke box (32) being located at described heat exchange area (3) top, be located at the lower smoke box (33) of described heat exchange area (3) bottom, the top of the body of heater corresponding with described heat exchange area (3), bottom is respectively equipped with the water inlet (35) with body of heater (1) ft connection, delivery port (34), be communicated with by boundling flue (36) between described upper smoke box (32) with described lower smoke box (33), described upper smoke box (32), lower smoke box (33), water jacket (31) is formed between boundling flue (36) and described body of heater, described upper smoke box (32) is communicated with by flue with described burner hearth (23), described lower smoke box (33) is communicated with the air-introduced machine (4) being located at body of heater outside by flue.
2. a kind of combustion formula biomass boiler according to claim 1, it is characterized in that: described upper smoke box (32) comprises the first upper smoke box (321) set gradually, second upper smoke box (322), described lower smoke box (33) comprises the first lower smoke box (331) set gradually, second lower smoke box (332), described first upper smoke box (321) is communicated with described burner hearth (23), described second lower smoke box (332) is communicated with described air-introduced machine (4), between described first upper smoke box (321) and described first lower smoke box (331), all be communicated with by described boundling flue (36) between described first lower smoke box (331) with described second upper smoke box (322) and between described second upper smoke box (322) with described second lower smoke box (332), make flue gas tortuous advance in described heat exchange area (3).
3. a kind of combustion formula biomass boiler according to claim 1, is characterized in that: the air outlet of described air-introduced machine (4) is connected with dust arrester (5).
4. a kind of combustion formula biomass boiler according to claim 1, is characterized in that: described fire grate (24) is casting furnace grate.
5. a kind of combustion formula biomass boiler according to claim 1, is characterized in that: the charging aperture place of described combustion chamber (21) is provided with rotary blade.
6. a kind of combustion formula biomass boiler according to claim 1, is characterized in that: the furnace body outer wall corresponding with described combustion chamber (21) is provided with can the finder (6) of switch.
7. a kind of combustion formula biomass boiler according to claim 1, is characterized in that: described feed arrangement (20) is auger type feed arrangement.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520457011.2U CN204756893U (en) | 2015-06-30 | 2015-06-30 | Interior burning formula biomass boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520457011.2U CN204756893U (en) | 2015-06-30 | 2015-06-30 | Interior burning formula biomass boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204756893U true CN204756893U (en) | 2015-11-11 |
Family
ID=54471596
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520457011.2U Expired - Fee Related CN204756893U (en) | 2015-06-30 | 2015-06-30 | Interior burning formula biomass boiler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204756893U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106123330A (en) * | 2016-07-07 | 2016-11-16 | 宁波中森生物质能源科技有限公司 | A kind of biomass thermal wind furnace |
| CN111120999A (en) * | 2019-12-31 | 2020-05-08 | 河北晔创科技有限公司 | Combustion furnace with high combustion rate and low coking |
| CN111120999B (en) * | 2019-12-31 | 2025-06-10 | 邯郸市晔创节能科技有限公司 | Combustion furnace with high combustion rate and low coking |
-
2015
- 2015-06-30 CN CN201520457011.2U patent/CN204756893U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106123330A (en) * | 2016-07-07 | 2016-11-16 | 宁波中森生物质能源科技有限公司 | A kind of biomass thermal wind furnace |
| CN111120999A (en) * | 2019-12-31 | 2020-05-08 | 河北晔创科技有限公司 | Combustion furnace with high combustion rate and low coking |
| CN111120999B (en) * | 2019-12-31 | 2025-06-10 | 邯郸市晔创节能科技有限公司 | Combustion furnace with high combustion rate and low coking |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20151111 Termination date: 20190630 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |