CN101708416B - Facility for efficiently eliminating harmful substances such as smoke, dust, sulphur, and the like in fume gas - Google Patents
Facility for efficiently eliminating harmful substances such as smoke, dust, sulphur, and the like in fume gas Download PDFInfo
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- CN101708416B CN101708416B CN2009102192310A CN200910219231A CN101708416B CN 101708416 B CN101708416 B CN 101708416B CN 2009102192310 A CN2009102192310 A CN 2009102192310A CN 200910219231 A CN200910219231 A CN 200910219231A CN 101708416 B CN101708416 B CN 101708416B
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- tower
- smoke
- dust
- wall
- facility
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- 239000000779 smoke Substances 0.000 title claims abstract description 49
- 239000000428 dust Substances 0.000 title claims abstract description 40
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims abstract description 13
- 239000005864 Sulphur Substances 0.000 title claims abstract description 13
- 239000000126 substance Substances 0.000 title claims abstract description 12
- 239000007789 gas Substances 0.000 title abstract description 10
- 239000003517 fume Substances 0.000 title abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 230000003009 desulfurizing effect Effects 0.000 claims description 18
- 235000019504 cigarettes Nutrition 0.000 claims description 7
- 241000397426 Centroberyx lineatus Species 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 239000004575 stone Substances 0.000 claims description 2
- 239000002956 ash Substances 0.000 abstract description 8
- 238000006477 desulfuration reaction Methods 0.000 abstract description 7
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 4
- 238000003287 bathing Methods 0.000 abstract description 2
- 230000008030 elimination Effects 0.000 abstract 4
- 238000003379 elimination reaction Methods 0.000 abstract 4
- 238000005507 spraying Methods 0.000 abstract 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 12
- 239000003546 flue gas Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 5
- 239000003245 coal Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
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Abstract
The invention relates to a facility for eliminating harmful substances such as smoke, dust, sulphur, and the like in fume gas. The facility mainly comprises a smoke elimination and desulfuration deduster and an induced draft fan, wherein the smoke elimination and desulfuration deduster comprises a deduster wall, a cylindrical inner cavity, a central shaft body and a guide fin fixed on the shaft body; a fume gas inlet of the cylindrical inner cavity is provided with a spraying device; the middle upper part of the deduster wall is provided with a plurality of dedusting and water spraying ports, and the lower part is provided with a draining hole. The smoke elimination and desulfuration deduster can be singly used and also be used by connecting with a desulfuration tower in series to achieve a better effect. The smoke elimination and desulfuration deduster achieves the purpose of eliminating pollutions of the harmful substances in the fume gas through impact, bathing and mechanical centrifugal force. The facility is suitable for various large, medium and small boilers and supporting facilities of industrial stoves and has obvious effect on eliminating the pollution of black smoke, ash and sulfur dioxide.
Description
Technical field
The present invention relates to a kind of environmental protection facility, specifically a kind of facility of the harmful substances such as middle cigarette, dust, sulphur that remove smoke.
Background technology
Be the boiler, Industrial Stoves etc. of fuel with the coal, have the cheap relatively characteristics of fuel cost, but owing to behind the coal combustion, contain a large amount of ashes, co in the high-temperature flue gas of generation
2, harmful substance such as co, slag, the dense black smoke of release causes severe contamination to environment.Eliminate or reduce the method for smoke pollution at present, mainly contain two kinds: dry method or wet method, pluses and minuses separately are as shown in the table.
Summary of the invention
The objective of the invention is to, provide a kind of efficiency of dust collection high, simple in structure, maintenance, easy to maintenance, the facility that removes smoke and pollute of long service life.
The present invention has been achieved in that dust remover capable of eliminating smoke and desulphation and air-introduced machine.Dust remover capable of eliminating smoke and desulphation is being fixed a center axis body by spiral guide vane by dedusting wall, cylindrical cavity and place, inner chamber axis and is being formed.The gas approach place of cylindrical cavity is provided with sprayer unit.The middle and upper part of dedusting wall is provided with a plurality of dedusting water jets, and the bottom is provided with osculum; The front and back of dust remover capable of eliminating smoke and desulphation are connected with the downtake pipe road with the boiler smoke pipeline respectively; Air-introduced machine is installed on the downtake pipe road.Said air-introduced machine: be to make pernicious gas become the power of air-flow, generation impulsive force and the centrifugal force of high-speed motion.
Between dust remover capable of eliminating smoke and desulphation and air-introduced machine, can increase a desulfurizing tower, this desulfurizing tower is made up of the tower axle at Ta Bi, tower chamber and place, axis, tower chamber; Spiral fin is equipped with on tower axle top, and reverse acting spiral shape fin is arranged at the top; The middle and upper part of tower wall is provided with a plurality of sulphur removal water jets, and the bottom is provided with the tower osculum.The bottom of this desulfurizing tower communicates with dust remover capable of eliminating smoke and desulphation, and top and second exhaust pipe road join, and air-introduced machine is installed on the second exhaust pipe road.
Operation principle of the present invention is:
Dust remover capable of eliminating smoke and desulphation is made up of inlet plenum, clean room, dewatering station.
1, inlet plenum: ash-laden gas quickens in import throat collapsible tube gradually, and when arriving the throat place, flue gas flow rate is up to 25-35m/s, and flue gas is strong turbulent motion.Being provided with press water in the throat position sprays into---and be the vaporific whole throat that is covered with, the flue gas of high-speed motion, grit break through the mist film and the coacervating large particle ash globule.Then, get in the clean room of dust remover capable of eliminating smoke and desulphation.
2, clean room: be the centrifugal facility of machinery.Be provided with the multilayer deflector in this clean room, shower is equipped with on its top, and the bottom contains ponding.Ash-laden gas gets into from import department, in the shape of a spiral upset.In whole flow process, the grit in the flue gas receives mechanical action of centrifugal force to get rid of Xiang Tabi, rushes at deflector and bottom ponding place, takes the ash discharge groove of intracavity bottom after being adhered to by moisture film to, discharges automatically through the water seal ash discharging hole.
3, dewatering station: purified gas gets into dewatering station and reduces the rotation flow velocity suddenly, makes the moisture in the flue gas can not get enough centrifugal force and sedimentation, and the ash discharge groove of the moisture after the sedimentation at the bottom of tower discharged by the water seal ash discharging hole automatically.Separate thereby reach carbonated drink, make the flue gas after the processing not be with water.
The present invention's dust remover capable of eliminating smoke and desulphation with the harmful substance in the flue gas, reaches the purpose of eliminating its pollution through impact, bathing and mechanical centrifugal force.This dust remover capable of eliminating smoke and desulphation can use separately, also can use with the desulfurizing tower polyphone, and the reducing smoke and dust and desulfurizing effect when polyphone uses is better.The present invention is applicable to the auxiliary facility of all kinds of large, medium and small type boilers and Industrial Stoves, and to eliminating black smoke, the pollution of grey dust, sulfur dioxide has fairly obvious effect.Probationary certificate, this dust remover capable of eliminating smoke and desulphation meets the requirement of emission standard of air pollutants for boilers GB13271-2001 class one zone fully.Also reached the requirement among " Industrial Boiler and stove wet process of FGD engineering legislation " HJ462-2009 fully.
When using dust remover capable of eliminating smoke and desulphation separately:
Smoke dust discharge concentration≤80mg/Nm
3
Efficiency of dust collection: >=98%
SO
2Concentration of emission≤100mg/Nm
3
Desulfuration efficiency: >=95%
Lingemann blackness≤1 grade
When dust remover capable of eliminating smoke and desulphation, the use of desulfurizing tower polyphone:
Smoke dust discharge concentration≤50mg/Nm
3
Efficiency of dust collection: >=99%
SO
2Concentration of emission≤50mg/Nm
3
Desulfuration efficiency: >=98%
Lingemann blackness≤1 grade
Description of drawings
Fig. 1. be overall structure sketch map of the present invention;
Fig. 2. be the structural representation of dust remover capable of eliminating smoke and desulphation;
Fig. 3. be the structural representation of desulfurizing tower.
Among the figure, the 1st, dust remover capable of eliminating smoke and desulphation, the 2nd, desulfurizing tower, 3-1,3-2 are respectively downtake pipe road and second exhaust pipe road discharge duct, the 4th, air-introduced machine; The 5th, dedusting wall, the 6th, center axis body, the 7th, spiral guide vane, the 8th, inner chamber, the 9th, osculum; The 10th, boiler smoke pipeline (being admission line), the 11st, dedusting water jet, the 12nd, tower wall, the 13rd, tower chamber, the 14th, tower axle; The 15th, spiral fin, the 16th, reverse acting spiral shape fin, the 17th, sulphur removal water jet, the 18th, tower osculum.
The specific embodiment
Below in conjunction with embodiments of the invention of accompanying drawing narration
The material of the main part of present embodiment (dedusting wall, center axis body, spiral fin, Ta Bi, tower axle, tower are used spiral fin) is numb stone, has characteristics such as quality is hard, acidproof, alkaline-resisting, wear-resisting.
The overall structure of present embodiment is as shown in Figure 1.Mainly form by dust remover capable of eliminating smoke and desulphation 1, desulfurizing tower 2 and air-introduced machine 4.The flue gas that coal-burning boiler produces under the draft of air-introduced machine, behind dust remover capable of eliminating smoke and desulphation, desulfurizing tower, gets into chimney and discharges.
The structure of dust remover capable of eliminating smoke and desulphation is as shown in Figure 2.Mainly form by dedusting wall 5, cylindrical cavity 8; On the wall at the gas approach place of cylindrical cavity 8, penstocks are housed, the press water of its ejection is the vaporific whole throat that is covered with, and the flue gas of high-speed motion, grit break through the mist film and the coacervating large particle ash globule.A center axis body 6 is being fixed at the place, axis of inner chamber; Center axis body 6 is being fixed a spirality guide vane 7.The middle and upper part of dedusting wall 5 is provided with a plurality of dedusting water jets 11, and the bottom is provided with osculum 9; The front and back of dust remover capable of eliminating smoke and desulphation 1 are connected with downtake pipe road 3-1 with boiler smoke pipeline 10 respectively; Air-introduced machine 4 is installed on the downtake pipe road 3-1.
The structure of desulfurizing tower is as shown in Figure 3.Desulfurizing tower 2 mainly is made up of the tower axle 14 at tower wall 12, tower chamber 13 and place, axis, tower chamber; Tower is equipped with spiral fin 15 in tower axle top, and reverse acting spiral shape fin 16 is arranged at the top; The middle and upper part of tower wall 12 is provided with a plurality of sulphur removal water jets 17, and the bottom is provided with tower osculum 18; The bottom of this desulfurizing tower 2 communicates with dust remover capable of eliminating smoke and desulphation 1, and top and second exhaust pipe road 3-2 join, and air-introduced machine 4 is installed on the second exhaust pipe road 3-2.Tower wall 12 inwalls have moisture film, the tower axle, and tower axle 14 outer walls have moisture film.
On the tower body inwall of spiral fin 15 belows, a plurality of independent sealing overflow tanks of a circle are arranged, each overflow tank has a feed pipe, when the overflow launder topped up with water, overflows to the tower body inwall of desulfurizing tower 2, makes the tower wall produce the layer of even moisture film.There is a groove at tower axle 14 middle parts, feed feed pipe, and the outer wall that after the groove topped up with water, flows to the tower axle forms moisture film.On the tower wall 12 of the top of reverse acting spiral shape fin 16, many lock tanks are arranged.On the last squarer wall of the reverse acting spiral shape fin 16 at desulfurizing tower 2 tops, have many vertical swallow-tail form lock tanks.Moisture flue gas is after reverse acting spiral shape fin 16 is arranged at the top; Produce centrifugal force, the moisture in the flue gas is got rid of on the cylindrical tower wall, many vertical swallow-tail form lock tanks; The water that gets rid of on the cylindrical tower wall is pinned; Flow to the bottom of tower, can not make the water generates secondary sputtered of getting rid of, thereby reach the effect of fume-dehydrating demisting to the tower wall.
Claims (5)
1. the facility of harmful substance cigarette, dust, sulphur is characterized in that: dust remover capable of eliminating smoke and desulphation (1) and air-introduced machine (4) are arranged in removing smoke; Dust remover capable of eliminating smoke and desulphation is made up of dedusting wall (5), cylindrical cavity (8), center axis body (6) and the spiral guide vane (7) that is fixed on this axis body; The gas approach place of cylindrical cavity (8) is provided with sprayer unit; The middle and upper part of dedusting wall (5) is provided with a plurality of dedusting water jets (11), and the bottom is provided with osculum (9); The front and back of dust remover capable of eliminating smoke and desulphation (1) are connected with downtake pipe road (3-1) with boiler smoke pipeline (10) respectively; Air-introduced machine (4) is installed on the downtake pipe road (3-1); Between dust remover capable of eliminating smoke and desulphation (1) and air-introduced machine (4), increase a desulfurizing tower (2), this desulfurizing tower is made up of the tower axle (14) at tower wall (12), tower chamber (13) and place, axis, tower chamber; Spiral fin (15) is housed on the tower axle, and reverse acting spiral shape fin (16) is arranged at the top; The middle and upper part of tower wall (12) is provided with a plurality of sulphur removal water jets (17), and the bottom is provided with tower osculum (18); The bottom of desulfurizing tower (2) communicates with dust remover capable of eliminating smoke and desulphation (1), and top and second exhaust pipe road (3-2) join, and air-introduced machine (4) is installed on the second exhaust pipe road (3-2); Tower wall (12) inwall has moisture film, and tower axle (14) outer wall has moisture film.
2. according to the facility of said remove smoke middle harmful substance cigarette, dust, sulphur of claim 1, it is characterized in that: on the tower body inwall of spiral fin (15) below, a plurality of independent sealing overflow tanks of a circle are arranged, each overflow tank has a feed pipe.
3. according to the facility of said remove smoke middle harmful substance cigarette, dust, sulphur of claim 1, it is characterized in that: there is a groove at tower axle (14) middle part, feeds feed pipe.
4. according to the facility of said remove smoke middle harmful substance cigarette, dust, sulphur of claim 1, it is characterized in that: on the tower wall (12) of the top of reverse acting spiral shape fin (16), many vertical swallow-tail forms lock tanks are arranged.
5. according to the facility of said remove smoke middle harmful substance cigarette, dust, sulphur of claim 2, it is characterized in that: the material of dedusting wall (5), center axis body (6), spiral guide vane (7), tower wall (12), tower axle (14) spiral fin (15), reverse acting spiral shape fin (16) is numb stone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009102192310A CN101708416B (en) | 2009-11-30 | 2009-11-30 | Facility for efficiently eliminating harmful substances such as smoke, dust, sulphur, and the like in fume gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009102192310A CN101708416B (en) | 2009-11-30 | 2009-11-30 | Facility for efficiently eliminating harmful substances such as smoke, dust, sulphur, and the like in fume gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101708416A CN101708416A (en) | 2010-05-19 |
| CN101708416B true CN101708416B (en) | 2012-11-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009102192310A Expired - Fee Related CN101708416B (en) | 2009-11-30 | 2009-11-30 | Facility for efficiently eliminating harmful substances such as smoke, dust, sulphur, and the like in fume gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101708416B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105817107A (en) * | 2016-05-12 | 2016-08-03 | 江苏迎阳无纺机械有限公司 | Dust-containing air water washing and dedusting device |
| CN107191957A (en) * | 2017-07-12 | 2017-09-22 | 容县润达家具有限公司 | A kind of processing unit of boiler exhaust gas |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3744220A (en) * | 1971-07-24 | 1973-07-10 | Siemens Ag | Device for imparting a twist to a flow of raw gas in a tornado flow separator |
| DE2249485B2 (en) * | 1972-10-10 | 1976-05-13 | Schlewitz, Armin, 6430 Bad Hersfeld | CYCLONE FOR DUST SEPARATION FROM HOT GASES |
| CN2164898Y (en) * | 1993-06-29 | 1994-05-18 | 周良才 | Vertical spiral waste gas cleaning device |
| CN2200752Y (en) * | 1994-10-14 | 1995-06-14 | 杨培灿 | Corrugated spray type smoke purifier |
| CN101254488A (en) * | 2007-11-30 | 2008-09-03 | 山东净化环保设备有限公司 | Whirlwind wet collector |
| CN201558645U (en) * | 2009-11-30 | 2010-08-25 | 龙波 | Facility for effectively removing harmful substances such as smoke, dust, sulfur and the like in flue gas |
-
2009
- 2009-11-30 CN CN2009102192310A patent/CN101708416B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3744220A (en) * | 1971-07-24 | 1973-07-10 | Siemens Ag | Device for imparting a twist to a flow of raw gas in a tornado flow separator |
| DE2249485B2 (en) * | 1972-10-10 | 1976-05-13 | Schlewitz, Armin, 6430 Bad Hersfeld | CYCLONE FOR DUST SEPARATION FROM HOT GASES |
| CN2164898Y (en) * | 1993-06-29 | 1994-05-18 | 周良才 | Vertical spiral waste gas cleaning device |
| CN2200752Y (en) * | 1994-10-14 | 1995-06-14 | 杨培灿 | Corrugated spray type smoke purifier |
| CN101254488A (en) * | 2007-11-30 | 2008-09-03 | 山东净化环保设备有限公司 | Whirlwind wet collector |
| CN201558645U (en) * | 2009-11-30 | 2010-08-25 | 龙波 | Facility for effectively removing harmful substances such as smoke, dust, sulfur and the like in flue gas |
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| Publication number | Publication date |
|---|---|
| CN101708416A (en) | 2010-05-19 |
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Granted publication date: 20121107 Termination date: 20181130 |