CN102022712A - Waste incineration waste heat boiler - Google Patents
Waste incineration waste heat boiler Download PDFInfo
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- CN102022712A CN102022712A CN 201010295326 CN201010295326A CN102022712A CN 102022712 A CN102022712 A CN 102022712A CN 201010295326 CN201010295326 CN 201010295326 CN 201010295326 A CN201010295326 A CN 201010295326A CN 102022712 A CN102022712 A CN 102022712A
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- burner hearth
- hearth
- described burner
- gas passage
- refuse incineration
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Abstract
The invention discloses a waste incineration waste heat boiler, which comprises a hearth, a hearth inlet and a hearth outlet, wherein the hearth inlet is arranged at the front end of a flue gas channel in the hearth; the hearth outlet is arranged at the tail end of the flue gas channel in the hearth; the flue gas channel in the hearth between the hearth inlet and the hearth outlet has a variable cross-section structure; the length L (meter) of the flue gas channel in the hearth is more than or equal to the result acquired by multiplying the maximum flow rate V (meter/second) of flue gas in the hearth by T (second), namely, L is more than or equal to V*T, wherein T is equal to 2 seconds; and an ammonia spray and denitrification system is arranged in the hearth. The waste incineration waste heat boiler makes wastes sufficiently burned and effectively reduces the emission of toxic and harmful substances; the hearth has a membrane type water-cooled wall structure and a membrane type water-cooled wall has remarkable sealing performance and high heat exchanging efficiency and prevents dust accumulation; and the waste incineration waste heat boiler has the characteristics of high using efficiency, long service life and the like.
Description
Technical field
The invention belongs to boiler manufacturing technology field, specifically, relate to refuse incineration exhaust-heating boiler.
Background technology
Garbage disposal has become a global problem, and countries in the world are all developed treatment facility and the method to rubbish one after another.At present, processing most countries to rubbish adopts refuse incineration exhaust-heating boiler that rubbish is carried out burning disposal, a kind of treatment technology that incineration treatment of garbage is the whole world present stage garbage disposal minimizing, resource, innoxious degree is the highest, and the heat energy that burn to produce can heat supply or generating, the inner poisonous and harmful element of rubbish obtains decomposing after the high temperature incineration process simultaneously, so incineration treatment of garbage is the effective technology that is fit to the big and medium-sized cities garbage disposal demand that Economic Development is rapid, land resource is nervous, garbage disposal is difficult.
Refuse incineration exhaust-heating boiler of the prior art, usually adopt common waste gas of incineration boiler to carry out, the burner hearth inside of described common waste gas of incineration boiler is the straight barrel type project organization that size diameter equates, and common waste gas of incineration boiler does not improve according to the characteristics of waste incineration and optimizes, and causes existing following many technical problems:
1, adopts existing waste gas of incineration boiler that rubbish is burned, can not adapt to the characteristics that refuse thermal value is low, moisture is high, usually cause waste incineration insufficient.
2, adopt existing waste gas of incineration boiler that rubbish is burned, existing waste gas of incineration boiler structurally can not fully satisfy the characteristics of incineration firing, usually produces a large amount of toxic and harmfuls.
3, adopt existing waste gas of incineration boiler that rubbish is burned, inefficiency, the time consuming time is long, disposal of refuse cost height.
Summary of the invention
Technical scheme provided by the invention technical problem to be solved is, adopt existing waste gas of incineration boiler that rubbish is burned, can not adapt to the characteristics that refuse thermal value is low, moisture is high, usually cause waste incineration insufficient, usually produce a large amount of toxic and harmfuls, inefficiency, the time consuming time is long, disposal of refuse cost high-technology problem, and refuse incineration exhaust-heating boiler is provided.
Technical scheme provided by the present invention is, refuse incineration exhaust-heating boiler, comprise burner hearth, burner hearth import department and furnace outlet place, described burner hearth import department is arranged on the front end of described burner hearth inner gas passage, described furnace outlet place is arranged on the end of described burner hearth inner gas passage, burner hearth inner gas passage between described burner hearth import department and furnace outlet place is made as variable section structure, the length L of described burner hearth inner gas passage (rice) multiply by T (second) more than or equal to flue gas Peak Flow Rate V (meter per second) in the described burner hearth, be L 〉=V * T, described T is 2 seconds; Be provided with spray ammonia denitrating system in the described burner hearth.
Described spray ammonia denitrating system is arranged on the middle part of described burner hearth, on the position of the interior flue gas flow rate maximum of described burner hearth.
The integral body of described burner hearth inner gas passage is the serpentine of cleanliness.
One end in the vertical direction of the close described burner hearth of described burner hearth inner gas passage import department has certain gradient.
Described gradient is meant an end of the close described burner hearth of described burner hearth inner gas passage import department and the angle of vertical direction, and described angle is 0 degree-60 degree.Preferred described angle is 30 degree-45 degree.
Described burner hearth inner gas passage is provided with " slimwaist type " structure near an end at described furnace outlet place.
Described burner hearth inner gas passage diminishes earlier near the cross section of an end at described furnace outlet place, it is big that the back becomes, and the front end at the minimum place of described burner hearth exhaust gases passes cross section and the angle of vertical direction are smaller or equal to the rear end at the minimum place of described burner hearth exhaust gases passes cross section and the angle on the vertical direction.
Described refuse incineration exhaust-heating boiler burner hearth is provided with fin panel casing, and described fin panel casing is constituted by some cooling water pipes and steel plate.
Institute's furnace depth adapts with the inverse-push inclined reciprocating fire grate width that is mated.
Adopt technical scheme provided by the present invention, can effectively solve and adopt existing waste gas of incineration boiler that rubbish is burned, it is low to adapt to refuse thermal value, the characteristics that moisture is high, usually cause waste incineration insufficient, usually produce a large amount of toxic and harmfuls, inefficiency, time consuming time is long, disposal of refuse cost high-technology problem, simultaneously, refuse incineration exhaust-heating boiler provided by the present invention has the rubbish of making and fully burns, effectively lower the poisonous and harmful substance discharging, burner hearth adopts film water cold wall structure, and the fin panel casing sealing property is remarkable, and the heat exchange efficiency height, also be difficult for dust stratification; The service efficiency height, characteristics such as long service life.
Description of drawings
In conjunction with the accompanying drawings, the present invention is described further:
Fig. 1 is a structural representation of the present invention;
Fig. 2 is Fig. 1 partial enlarged drawing-spray ammonia denitrating system;
Wherein, 1 is burner hearth; 2 is burner hearth import department; 3 is the furnace outlet place; 4 is slimwaist type; 5 is the inverse-push inclined reciprocating fire grate, and 6 are spray ammonia denitrating system.
The specific embodiment
Shown in Fig. 1-2, design of the present invention provides a kind of waste gas of incineration boiler that can adapt to the characteristics that the house refuse calorific value is low, moisture is high, waste gas of incineration boiler of the present invention adopts the burning facility of international advanced technology, and on burner hearth 1 project organization, take into full account the characteristics of incineration firing, consider the degree of filling of flue gas in burner hearth 1 to greatest extent, prevent that pernicious gas from producing, and boiler is to the influence of surrounding environment health generation.
Technical scheme provided by the present invention is a refuse incineration exhaust-heating boiler, comprise burner hearth 1, burner hearth import department 2 and furnace outlet place 3, described burner hearth import department 2 is arranged on the front end of described burner hearth 1 inner gas passage, described furnace outlet place 3 is arranged on the end of described burner hearth 1 inner gas passage, burner hearth 1 inner gas passage between described burner hearth import department 2 and furnace outlet place 3 is made as variable section structure, the length L (rice) of described burner hearth 1 inner gas passage multiply by T (second) more than or equal to flue gas Peak Flow Rate V (meter per second) in the described burner hearth 1, be L 〉=V * T, described T is 2 seconds.
Described burner hearth 1 inner gas passage is made as variable section structure, has guaranteed that flue gas satisfies the degree of filling of burner hearth 1 to greatest extent in the waste gas of incineration boiler, satisfy the abundant burning of rubbish to greatest extent.The length L (rice) of burner hearth 1 inner gas passage multiply by T (second) more than or equal to flue gas Peak Flow Rate V (meter per second) in the described burner hearth 1, be L 〉=V * T, guarantee that to greatest extent the time of flue gas in burner hearth 1 was above 2 seconds, when even flue gas flow rate is maximum, can guarantee that also the time of flue gas in burner hearth 1 equals or exceeds 2 seconds, this structure has guaranteed the decomposition of pernicious gas (particularly dioxin).Highly the decomposition that prevents pernicious gas (particularly dioxin) is considered in design, and flue gas will be more than the time of staying 2s in stove.
Be provided with spray ammonia denitrating system 6 in the described burner hearth 1.Described spray ammonia denitrating system 6 is arranged on the middle part of described burner hearth 1, on the position of described burner hearth 1 interior flue gas flow rate maximum.Spray ammonia denitrating system 6 (SNCR) are set in the described burner hearth 1 carry out non-selective catalytic reduction reaction, reduce NOx content in the flue gas.Described spray ammonia denitrating system 6 (SNCR) is arranged on the place of described burner hearth 1 middle part flue gas flow rate maximum, helps carrying out catalytic reduction reaction, helps reducing NOx content in the flue gas, helps the abundant burning of rubbish.
The integral body of described burner hearth 1 inner gas passage is the serpentine of cleanliness, and this structure has guaranteed that the circulation of flue gas in burner hearth 1 is smooth and easy.
One end in the vertical direction of the close described burner hearth of described burner hearth 1 inner gas passage import department 2 has certain gradient.Described gradient is meant an end of the close described burner hearth of described burner hearth 1 inner gas passage import department 2 and the angle of vertical direction, and described angle is 0 degree-60 degree.Preferred described angle is 30 degree-45 degree.To be that exhaust gases passes is whole have certain included angle with vertical direction to described gradient, and the formation of this angle specifically can realize according to the outermost end outline line of the cross section of this exhaust gases passes vertical direction and the angle of vertical direction.This structure has guaranteed that flue gas satisfies the degree of filling of burner hearth 1 to greatest extent in the waste gas of incineration boiler, satisfy the abundant burning of rubbish to greatest extent.
Described burner hearth 1 inner gas passage is provided with " slimwaist type 4 " structure near an end at described furnace outlet place 3.Described burner hearth 1 inner gas passage diminishes earlier near the cross section of an end at described furnace outlet place 3, it is big that the back becomes, and the front end (outline line of the vertical direction of exhaust gases passes outermost end) at the minimum place of described burner hearth 1 exhaust gases passes cross section and the angle of vertical direction are smaller or equal to the angle on the rear end (outline line of the vertical direction of exhaust gases passes outermost end) at the minimum place of described burner hearth 1 exhaust gases passes cross section and the vertical direction.This structure has guaranteed backflow, the relatively circulation of flue gas in burner hearth 1, has guaranteed that flue gas satisfies the degree of filling of burner hearth 1 to greatest extent in the waste gas of incineration boiler, satisfy the abundant burning of rubbish to greatest extent.
Described refuse incineration exhaust-heating boiler burner hearth 1 is provided with fin panel casing, and described fin panel casing is constituted by some cooling water pipes and steel plate.Refuse incineration exhaust-heating boiler burner hearth 1 adopts film water cold wall structure, and the fin panel casing sealing property is remarkable, and the heat exchange efficiency height, also is difficult for dust stratification.
Institute's burner hearth 1 degree of depth adapts with inverse-push inclined reciprocating fire grate 5 width that mated.Described refuse incineration exhaust-heating boiler cooperates with inverse-push inclined reciprocating fire grate 5, and the design on burner hearth 1 degree of depth is complementary the two.
The foregoing description only is a most preferred embodiment of the present invention, and any deformation design scheme in the present invention conceives all is protection scope of the present invention.
Claims (10)
1. refuse incineration exhaust-heating boiler, comprise burner hearth (1), burner hearth import department (2) and furnace outlet place (3), described burner hearth import department (2) is arranged on the front end of described burner hearth (1) inner gas passage, described furnace outlet place (3) is arranged on the end of described burner hearth (1) inner gas passage, it is characterized in that, burner hearth (1) inner gas passage between described burner hearth import department (2) and furnace outlet place (3) is made as variable section structure, the length L (rice) of described burner hearth (1) inner gas passage multiply by T (second) more than or equal to described burner hearth (1) interior flue gas Peak Flow Rate V (meter per second), be L 〉=V * T, described T is 2 seconds; Be provided with spray ammonia denitrating system (6) in the described burner hearth (1).
2. refuse incineration exhaust-heating boiler according to claim 1 is characterized in that, described spray ammonia denitrating system (6) is arranged on the middle part of described burner hearth (1), on the position of the interior flue gas flow rate maximum of described burner hearth (1).
3. refuse incineration exhaust-heating boiler according to claim 1 and 2 is characterized in that, the integral body of described burner hearth (1) inner gas passage is the serpentine of cleanliness.
4. refuse incineration exhaust-heating boiler according to claim 3 is characterized in that, described burner hearth (1) inner gas passage has certain gradient near an end in the vertical direction of described burner hearth import department (2).
5. refuse incineration exhaust-heating boiler according to claim 4 is characterized in that, described gradient is meant described burner hearth (1) inner gas passage near an end of described burner hearth import department (2) and the angle of vertical direction, and described angle is 0 degree-60 degree.
6. refuse incineration exhaust-heating boiler according to claim 5 is characterized in that, described angle is 30 degree-45 degree.
7. according to claim 4 or 5 or 6 described refuse incineration exhaust-heating boilers, it is characterized in that described burner hearth (1) inner gas passage is provided with " slimwaist type (4) " structure near an end at described furnace outlet place () 3.
8. according to claim 4 or 5 or 6 described refuse incineration exhaust-heating boilers, it is characterized in that, described burner hearth (1) inner gas passage diminishes earlier near the cross section of an end at described furnace outlet place (3), it is big that the back becomes, and the front end at the minimum place of described burner hearth (1) exhaust gases passes cross section and the angle of vertical direction are smaller or equal to the rear end at the minimum place of described burner hearth (1) exhaust gases passes cross section and the angle on the vertical direction.
9. according to any described refuse incineration exhaust-heating boiler of claim 1-8, it is characterized in that described fin panel casing is constituted by some cooling water pipes and steel plate.
10. refuse incineration exhaust-heating boiler according to claim 9 is characterized in that, institute's burner hearth (1) degree of depth adapts with inverse-push inclined reciprocating fire grate (5) width that is mated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010295326 CN102022712A (en) | 2010-09-26 | 2010-09-26 | Waste incineration waste heat boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010295326 CN102022712A (en) | 2010-09-26 | 2010-09-26 | Waste incineration waste heat boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102022712A true CN102022712A (en) | 2011-04-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010295326 Pending CN102022712A (en) | 2010-09-26 | 2010-09-26 | Waste incineration waste heat boiler |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107166405A (en) * | 2017-06-26 | 2017-09-15 | 浙江伟明环保股份有限公司 | A kind of refuse incineration smoke processing system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3995567A (en) * | 1975-06-20 | 1976-12-07 | Enertherm, Inc. | Waste fuel incinerator and pollutant removal system |
| CN1061915A (en) * | 1990-07-13 | 1992-06-17 | 日立造船株式会社 | Process for simultaneously removing sulfur and nitrogen in furnace |
| CN1820823A (en) * | 2006-01-19 | 2006-08-23 | 同济大学 | Medium and high temperature smoke denitrating method |
| CN201448817U (en) * | 2009-04-09 | 2010-05-05 | 安徽金鼎锅炉股份有限公司 | Waste heat steam boiler for reciprocating grate residue incineration |
| CN201992661U (en) * | 2010-09-26 | 2011-09-28 | 安徽金鼎锅炉股份有限公司 | Novel garbage burning waste heat boiler |
-
2010
- 2010-09-26 CN CN 201010295326 patent/CN102022712A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3995567A (en) * | 1975-06-20 | 1976-12-07 | Enertherm, Inc. | Waste fuel incinerator and pollutant removal system |
| CN1061915A (en) * | 1990-07-13 | 1992-06-17 | 日立造船株式会社 | Process for simultaneously removing sulfur and nitrogen in furnace |
| CN1820823A (en) * | 2006-01-19 | 2006-08-23 | 同济大学 | Medium and high temperature smoke denitrating method |
| CN201448817U (en) * | 2009-04-09 | 2010-05-05 | 安徽金鼎锅炉股份有限公司 | Waste heat steam boiler for reciprocating grate residue incineration |
| CN201992661U (en) * | 2010-09-26 | 2011-09-28 | 安徽金鼎锅炉股份有限公司 | Novel garbage burning waste heat boiler |
Non-Patent Citations (1)
| Title |
|---|
| 《科技信息》 20091231 孙大玺等 垃圾焚烧炉技术探讨－加拿大某垃圾焚烧炉项目简介 , 第35期 2 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107166405A (en) * | 2017-06-26 | 2017-09-15 | 浙江伟明环保股份有限公司 | A kind of refuse incineration smoke processing system |
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Application publication date: 20110420 |