CN1201125A - Technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying for coal-burning boiler and furnace - Google Patents
Technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying for coal-burning boiler and furnace Download PDFInfo
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- CN1201125A CN1201125A CN 98110263 CN98110263A CN1201125A CN 1201125 A CN1201125 A CN 1201125A CN 98110263 CN98110263 CN 98110263 CN 98110263 A CN98110263 A CN 98110263A CN 1201125 A CN1201125 A CN 1201125A
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- flue gas
- multitube
- boiler
- force
- stainless
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- 239000000428 dust Substances 0.000 title claims abstract description 19
- 239000000779 smoke Substances 0.000 title claims description 13
- 230000003009 desulfurizing effect Effects 0.000 title claims description 7
- 238000000746 purification Methods 0.000 claims abstract description 29
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 22
- 239000010935 stainless steel Substances 0.000 claims abstract description 22
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000003546 flue gas Substances 0.000 claims abstract description 20
- 239000007921 spray Substances 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 238000000926 separation method Methods 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000002253 acid Substances 0.000 claims description 14
- 239000000853 adhesive Substances 0.000 claims description 13
- 230000001070 adhesive effect Effects 0.000 claims description 13
- 239000004570 mortar (masonry) Substances 0.000 claims description 13
- 230000000694 effects Effects 0.000 claims description 8
- 230000007613 environmental effect Effects 0.000 claims description 7
- 239000010865 sewage Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- 239000003500 flue dust Substances 0.000 claims 2
- 238000006477 desulfuration reaction Methods 0.000 abstract description 2
- 230000023556 desulfurization Effects 0.000 abstract description 2
- 239000004927 clay Substances 0.000 abstract 1
- 239000003245 coal Substances 0.000 description 11
- 241001122767 Theaceae Species 0.000 description 7
- 238000007599 discharging Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000003822 epoxy resin Substances 0.000 description 3
- 229920000647 polyepoxide Polymers 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000002000 scavenging effect Effects 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000005357 flat glass Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 230000002335 preservative effect Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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Abstract
The smoke-eliminating dust-removing desulfurization and denitrification equipment for coal-fired boiler and kiln furnace is characterized by that it possesses a waist drum round Venturi tube primary purifier, an acid-resisting clay multi-tube jetting secondary purification tower, some stainless steel tube jet nozzles and swirl atomized spray injector, and uses the blow-off alkaline rinse to jet dust-bearing flue gas, and makes the cleaned flue gas pass through gas-liquid separation demister and discharges one, through chimney, into atmosphere by means of induced draft fan of boiler.
Description
The present invention relates to Industrial Boiler kiln heating boiler, tea furnace tail flue gas smoke elimination, dedusting, take off SO
2Take off NO
xTechnique device, particularly for the spreader stoker boliler, CFBB, fluidized bed furnace, coal-powder boiler, reciprocating-grate boiler, the hand-fired boiler that solve severe overweight exhaust emission environment, all kinds of model Industrial Stoves, life tea furnace have great popularizing value, and be better for the grate firing type chain grate boiler clean-up effect of all kinds of models.
China is a country based on coal, coal is in China's primary energy is produced and consumed, account for more than 70% always, along with expanding economy, the coal in China consumption increases year by year, consumes 1,500,000,000 tons in coal every year approximately, the power station all kinds of life tea furnaces of large medium-size boiler Industrial Stoves that China's great majority use sulphur coal do not have the desulfurization facility, technology falls behind, coal consumption height, SO
2Middle-size and small-size power station that discharge capacity is big and Industrial Stoves are also very general, and life tea furnace, resident's cooking stove in each city, the whole nation still use diffusing coal, and this has just caused China SO
2Discharge capacity is the gesture of increase more and more year by year.Station boiler is the SO of Chinese future maximum according to statistics
2Emission source, 95 years national SO
2Discharge capacity is 8,200,000 tons, SO in 2000
2Discharge capacity will reach 1,100 ten thousand tons, by 2010, and SO
2About 1,300 ten thousand tons of discharge capacitys.Industrial boilers in China nineteen ninety-five whole nation boiler is approximately 49.92 ten thousand tons, and production capacity is 119.81 ten thousand steaming tons, and national Industrial Boiler coal consumption was about 4.3 hundred million tons in 95 years, discharging SO
2Be 8,050,000 tons,, will reach 140-150 ten thousand to the production capacity of Industrial Boiler in 2000 and steam ton that coal consumption will reach 4.8 hundred million tons, then SO according to dynamo-electric portion scholarly forecast
2Generation is approximately 9,000,000 tons, will reach 1,800,000 to the production capacity of Industrial Boiler in 2010 and steam ton, and coal consumption will reach 5.2 hundred million tons, discharging SO
2About 9,750,000 tons.Industrial Stoves: nearly 180,000 of 1995 Industrial Stoves, more than 200,000,000 ton of year coal consumption, SO
2Discharge capacity is approximately 3,020,000 tons, reaches 21.6 ten thousand, SO to Industrial Stoves in 2000
2Discharge capacity reaches about 1,360 ten thousand tons, because Industrial Stoves have a large capacity and a wide range, China does not also control SO at present preferably
2Technology.According to SO during the statistics " eight or five " of national each province and city environmental administration
2Mean annual concentration superstate secondary standard, average daily concentration surpasses grade III Standard, visible China city SO
2Pollute quite serious, SO
2The task of discharging is very arduous, and " national environmental protection the ninth five-year plan and long-range target in 2010 " of Chinese government's promulgation proposed the enforcement period of the ninth five-year plan whole nation total emissions of major pollutants control plan.Chinese Government has further established environment and sustained economic development ten big countermeasure strategy and policy, and " the Chinese Agenda 21 " of State Council approved all clearly proposes to solve environment and development and will rely on scientific and technological advances.
Purpose of the present invention is the serious coal-fired power station boiler of contaminated solution, spreader stoker boliler, CFBB, fluidized bed furnace, coal-powder boiler, reciprocating-grate boiler, hand-fired boiler, all kinds of model Industrial Stoves, life tea furnace technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying prior art deficiency have proposed the better economical and practical purification techniques device of one kind of multiple functional effects.This device and existing country " 95 " national science and technology tackling key problem environmental protection project, the best practical technology that national environmental protection is promoted is compared, has the structural principle novelty, volume is little, and the manufacturing cost cost is low, and operating maintenance is easy to use, operating cost is few, comprehensive purifying rate height, acid-alkali-corrosive-resisting, characteristics such as long service life.
Technical scheme of the present invention realizes by following manner, this device has adopted the circular Venturi tube first class purification of waist drum device, the acid resistant adhesive mortar multitube swashs the spray tower second cleaner by force, several stainless-steel pipe jet blowers, the whirlpool spray nozzle, the gas-liquid separation demister utilizes boiler blow-off waste water alkalies to swash ash-laden gas by force, thereby reaches desirable clean-up effect.It is formed structure and mainly contains: boiler, kiln, the ash-laden gas that the tea furnace burning is discharged enters the circular Venturi tube first class purification device (2) of waist drum by the top of flue tube (1), in collapsible tube (3), set up shallow plate (4), to increase effective contact area of flue gas and liquid, its concrete structure is to establish the spout place that stainless steel tube water supply endless tube is distributed in several stainless-steel pipe jet blowers (5), be provided with shallow plate (4), shallow plate (4) can be flat glass or acidproof brick, some shallow plates (4) are along discharging successively on every side, with epoxy resin shallow plate (4) is bonded on the shape base plate of garden, the akaline liquid of stainless-steel pipe jet blower (5) ejection is fan-shaped shallow opening after shallow plate (4) reflection, contacts with flue gas then; Increased effective contact area greatly.Impact atomizing through top stainless-steel pipe whirlpool spray nozzle (6), the drop that injector (6) gushes out becomes thinner droplet by the further atomizing of trunnion (7) under high velocity air impacts, gas is saturated by water institute fully simultaneously, the air film of grit surface attachment breaks through, make grit by water-wet, therefore fierce inertia magnetic taking place between grit and drop hitting effects such as interception cohesion, make grit and harmful substance in the flue gas be caught absorption by abundant atomizing and foam, flue gas is cooled and carries out desulphurization reaction, grit and SO in coalescence and the absorption flue gas
2, NO
xAfter the alkaline matter effect in harmful substance and the waste water, fall into circular water seal tank (11) with waste water from the central tube (10) in the sharp by force spray tower second cleaner of anemostat (8) inflow acid resistant adhesive mortar multitube and enter sewage water seal tank (12).Because of first class purification device inwall in the circular Venturi tube of waist drum is subjected to washing away of air blast, acid and alkali corrosion is serious, so connect glass cermaic plate with epoxy resin lining at trunnion (7) inwall, at collapsible tube (3) and anemostat (8) inwall epoxy resin lining cutting acid-proof ceramic tile, smear acid resistant adhesive mortar at the circular water seal tank of central tube (10) (11) inside and outside wall.Scavenging solution flows to several stainless-steel pipe jet blowers (5) of top stainless-steel pipe whirlpool spray nozzle (6) by stainless steel feed pipe (13) and realizes first class purification.Swash spray tower (9) top remittance locellus by force through the acid resistant adhesive mortar multitube again by first class purification device flue gas after being purified and be distributed in the multitube (14) that several acid resistant adhesive mortars of spray tower inner periphery are made, the scavenging solution that will have pressure by stainless steel water supply endless tube (15) is distributed in the little flue gas stream that several stainless-steel pipe whirlpool spray nozzles (16) swash by force in several multitubes (14) of cutting apart and realizes the meticulous purification of secondary again, in several multitubes, contacted micronic dust in absorption liquid and the flue gas and SO fully
2, NO
xHarmful substance enters sewage water seal tank (12), meanwhile with liquid-gas ratio be generally 1.5 '/
M3Scavenging solution removed and cut material SO
2, NO
xLower stream of airflow speed is dwindled the rise with pressure in spray tower second cleaner (9), make this with the grit be the cohesion of the nuclei of condensation take place faster, be condensed into the dust-laden drop of big grain, entering gas-liquid separation demister (17) whirlpool catches, thereby obtain better purification efficiency, the gas-liquid separation demister bottom is established water seal tank (18), for guarantee service life of equipment spray tower second cleaner (9) and gas-liquid separation demister (17) inner surface with wire netting, reinforcing bar in the preservative treatment of lined with diabase acid resistant adhesive mortar.Purifying the clean flue gas reached GB13271-91 atmosphere pollution I class area discharge standard through second cleaner sends into window chimney (20) by boiler induced-draft fan (19) and enters atmosphere.
The typical embodiment of its clean-up effect has: (1) is applied on the DHF29-1.6/150/90 CFBB and tests; Through the test of cleaner supervision and inspection center, State Bureau of Environmental Protection Beijing, lingemann blackness is dropped to below 1 grade by original 4-5 level; Smoke dust discharge concentration is by boiler export original concentration 14875
Mg/
Nm3, drop to 97
Mg/
Nm3, efficiency of dust collection reaches 99.3%; SO
2Purification efficiency reaches more than 88%, SO
2Concentration of emission is 148
Mg/
Nm3NO
xPurification efficiency reaches more than 76%.(2) test through being applied on the SZD10-25 forward-moving grate spreader stoker boliler; Lingemann blackness is dropped to below 1 grade by original 4-5 level; Smoke dust discharge concentration is by boiler export original concentration 15000
Mg/
Nm3Drop to 80.1
Mg/
Nm3, efficiency of dust collection reaches 99.2%; SO
2Purification efficiency reaches more than 92%; SO
2Concentration of emission is 49.6
Mg/
Nm3NO
xPurification efficiency reaches more than 78%.(3) through being applied in combustion test on the SZD20-13 forward-moving grate spreader stoker boliler; Lingemann blackness is dropped to below 1 grade by original 4-5 level; Smoke dust discharge concentration is by boiler export original concentration 15000
Mg/
Nm3Drop to 67.4
Mg/
Nm3Efficiency of dust collection reaches 99.6%; SO
2Purification efficiency reaches more than 96%, SO
2Concentration of emission is 29.9
Mg/
Nm3NO
xPurification efficiency reaches more than 80%.(4) test through being applied on the Industrial Stoves; Lingemann blackness is dropped to below 1 grade by original Pyatyi, and smoke dust discharge concentration reaches 100
Mg/
Nm3Below, efficiency of dust collection reaches more than 98%; SO
2Purification efficiency reaches 90% above NO
xPurification efficiency reaches more than 78%.(5) through being applied in evidence on the life tea furnace; Lingemann blackness reaches below 1 grade, and smoke dust discharge concentration reaches 100
Mg/
Nm3Below, efficiency of dust collection reaches more than 98%, SO
2Purification efficiency reaches more than 96%; NO
xPurification efficiency reaches more than 80%.
Description of drawings: Fig. 1 is this structural representation; Fig. 2 is the collapsible tube enlarged drawing.(1) flue tube, the circular Venturi tube first class purification of (2) waist drum device; (3) collapsible tube; (4) shallow plate; (5) stainless-steel pipe jet blower; (6) stainless-steel pipe whirlpool spray nozzle; (7) trunnion; (8) anemostat; (9) the acid resistant adhesive mortar multitube swashs the spray tower second cleaner by force; (10) central tube; (11) circular water seal tank; (12) sewage water seal tank; (13) stainless steel feed pipe; (14) acid resistant adhesive mortar multitube; (15) stainless steel water supply endless tube; (16) stainless-steel pipe whirlpool spray nozzle; (17) gas-liquid separation demister; (18) water seal tank; (19) boiler induced-draft fan; (20) window chimney.
Claims (4)
1, the coal-burning boiler and furnace multitube swashs the formula technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying by force, and by the circular Venturi tube first class purification of waist drum device, the acid resistant adhesive mortar multitube swashs the spray tower second cleaner by force, the gas-liquid separation demister, and boiler induced-draft fan constitutes package unit; It is characterized in that the circular Venturi tube first class purification device (2) of waist drum, in collapsible tube (3), set up several stainless-steel pipe jet blower (5) stainless-steel pipe whirlpool spray nozzles (6) of shallow plate (4), central tube (10), circular water seal tank (11) is realized first class purification; Swash spray tower second cleaner (9) by force through the acid resistant adhesive mortar multitube again, in establish several acid resistant adhesive mortar multitubes (14) and stainless-steel pipe spray nozzle (16) is housed swashs flue gas by force and realize the meticulous purification of secondary, flue dust and harmful substance enter sewage water seal tank (12), have reached the secondary purification effect; The clean flue gas that purifies is through gas-liquid separation demister (17), water seal tank (18), remove the drop in the flue gas after, the clean flue gas that will reach environmental emission standard enters atmosphere by boiler induced-draft fan.
2, swash the formula technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying by force according to right 1 described coal-burning boiler and furnace multitube, it is characterized in that the circular Venturi tube first class purification device (2) of waist drum, in collapsible tube (3), set up several stainless-steel pipe jet blower (5) stainless-steel pipe whirlpool spray nozzles (6) of shallow plate (4), central tube (10), circular water seal tank (11) is realized first class purification.
3, swash the formula technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying by force according to right 1 described coal-burning boiler and furnace multitube, it is characterized in that the acid resistant adhesive mortar multitube swashs spray tower second cleaner (9) by force, in establish several acid resistant adhesive mortar multitubes (14) and stainless-steel pipe injector (16) is housed swashs flue gas by force and realize the meticulous purification of secondary, flue dust and harmful substance enter sewage water seal tank (12), have reached the secondary purification effect.
4, swash the formula technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying by force according to right 1 described coal-burning boiler and furnace multitube, the clean flue gas that it is characterized in that purifying is through gas-liquid separation demister (17), water seal tank (18), after removing the drop in the flue gas, the clean flue gas that will reach environmental emission standard enters atmosphere by boiler induced-draft fan.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98110263 CN1061430C (en) | 1998-06-05 | 1998-06-05 | Technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying for coal-burning boiler and furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98110263 CN1061430C (en) | 1998-06-05 | 1998-06-05 | Technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying for coal-burning boiler and furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1201125A true CN1201125A (en) | 1998-12-09 |
| CN1061430C CN1061430C (en) | 2001-01-31 |
Family
ID=5220326
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 98110263 Expired - Lifetime CN1061430C (en) | 1998-06-05 | 1998-06-05 | Technical apparatus of smoke preventing and dust controlling, desulfurizing and denitrifying for coal-burning boiler and furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1061430C (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103214118A (en) * | 2013-04-03 | 2013-07-24 | 国家电网公司 | Method for treating waste water by utilizing dust-containing smoke gas of coal-fired boiler |
| CN113464837A (en) * | 2021-09-01 | 2021-10-01 | 江苏新鹏重型机电制造有限公司 | Auxiliary air inlet structure with vortex type pressure stabilizing and flow guiding function for desulfurization and denitrification and method |
-
1998
- 1998-06-05 CN CN 98110263 patent/CN1061430C/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103214118A (en) * | 2013-04-03 | 2013-07-24 | 国家电网公司 | Method for treating waste water by utilizing dust-containing smoke gas of coal-fired boiler |
| CN103214118B (en) * | 2013-04-03 | 2015-04-01 | 国家电网公司 | Method for treating waste water by utilizing dust-containing smoke gas of coal-fired boiler |
| CN113464837A (en) * | 2021-09-01 | 2021-10-01 | 江苏新鹏重型机电制造有限公司 | Auxiliary air inlet structure with vortex type pressure stabilizing and flow guiding function for desulfurization and denitrification and method |
| CN113464837B (en) * | 2021-09-01 | 2021-11-19 | 江苏新鹏重型机电制造有限公司 | Auxiliary air inlet structure with vortex type pressure stabilizing and flow guiding function for desulfurization and denitrification and method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1061430C (en) | 2001-01-31 |
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| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| AR01 | Abandonment of patent right to avoid double patenting |
According to article 9 of the patent law and article 12 of the detailed rules for the implementation of the patent law: 98110263.8 of the invention patents in this issue as a notice of authorization, and at the same time corresponding to the 98221387.5 utility model patent to be given up, and in the 17 volume of the 5 issue of the new type of communique on the patent right to abandon the announcement. |
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| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20081226 Address after: Block A, building 1, building 6, building 2703, Xueyuan Road, Beijing, Haidian District Patentee after: Beijing Sheng Xing environmental protection boiler hi tech Limited by Share Ltd. Address before: Shandong Province, Feicheng City, new energy saving and environmental protection equipment factory (Feicheng City Tai Ping Road No. 011 Taitung TV) Patentee before: Liu Zengchun |
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| ASS | Succession or assignment of patent right |
Owner name: BEIJING SHENGXING ENVIRONMENTAL PROTECTION BOILER Free format text: FORMER OWNER: LIU ZENGCHUN Effective date: 20081226 |
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| DD01 | Delivery of document by public notice |
Addressee: Beijing Sheng Xing environmental protection boiler hi tech Limited by Share Ltd. Document name: Notification to Pay the Fees |
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Addressee: Beijing Sheng Xing environmental protection boiler hi tech Limited by Share Ltd. Document name: Notification of Decision on Request for Restoration of Right |
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Granted publication date: 20010131 |