CN203264541U - System capable of combining oxygen-enriched combustion supporting with flue gas desulfurization and denitration for industrial kiln - Google Patents
System capable of combining oxygen-enriched combustion supporting with flue gas desulfurization and denitration for industrial kiln Download PDFInfo
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- CN203264541U CN203264541U CN2013200943904U CN201320094390U CN203264541U CN 203264541 U CN203264541 U CN 203264541U CN 2013200943904 U CN2013200943904 U CN 2013200943904U CN 201320094390 U CN201320094390 U CN 201320094390U CN 203264541 U CN203264541 U CN 203264541U
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- desulfurization
- oxygen
- flue gas
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- denitrification
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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Abstract
The utility model discloses a system capable of combining oxygen-enriched combustion supporting with flue gas desulfurization and denitration for an industrial kiln. The system is mainly characterized in that the industrial kiln is connected with a dust remover; the dust remover is connected with a chimney through a desulfurization and denitration reaction tower; the desulfurization and denitration reaction tower is connected with an ozone generation device; the ozone generation device is connected with an oxygen-enriched generation device; the oxygen-enriched generation device is connected with a mixed air proportioning device; the mixed air proportioning device is connected with a combustion supporting nozzle in the industrial kiln. Through the system, an oxygen-enriched combustion supporting technology is combined with a flue gas desulfurization and denitration technology of the industrial kiln for the first time. The system is reasonable in process route, high in desulfurization and denitration efficiency, high in combustion efficiency and high in utilization rate of a desulfurization and denitration absorbing agent; the consumption of fuel such as coal is effectively reduced; the yield of the kiln is improved. The clinker firing quality of a cement kiln in the industrial kiln is effectively improved, and the 3-day strength and 28-day strength of finished cement can be improved.
Description
Technical field
The utility model relates to a kind of oxygen-enriched combustion-supporting of Industrial Stoves and flue gas desulfurization, denitrification apparatus.
Background technology
The exhaust emissions such as China's Industrial Stoves such as cement kiln, glass furnace, furnace are serious at present, cement industry adopts dry cement production line mostly, glass furnace adopts float line, the hear rate value that the new type dry kiln per kilogram that moves now be who knows is all at 3000-4000KJ, be 102.5-136.7 kilograms of standard coal/tons (every kilogram of mark coal low heating value is 7000 kilocalories), the energy saving space is larger.The NO of national cement industry of while
XDischarge capacity accounts for national industrial NO near 2,200,000 tons
X10% of total emission volumn is only second to power industry and motor-vehicle tail-gas, occupies the 3rd, NO
XConcentration of emission is 600-900mg/Nm approximately
3Simultaneously, glass furnace is about 10,000 tons, SO at statistics plate glass kiln discharge quantity of particulate matter in 2008
2Be about 150,000 tons, NO
XBe about 140,000 tons, this shows, SO
2And NO
XIt is the important pollution of glass furnace.In order to realize a series of energy-saving and emission-reduction indexs, force industrial Industrial Stoves to use enterprise improve its production technology or employ new technology, operable before the energy-saving square appearance is industrial Industrial Stoves rich Combustion Technics, is generally adopting the reaction of SNCR(SNCR aspect industrial waste gas of industrial kiln and furnace nitrogen oxide removing) or the denitration technology of SCR method.the Chinese utility model patent of at present existing publication number CN 101407381A and publication number CN 101053747A, they have proposed respectively " a kind of oxygen-enriched burning process and device thereof that improves the cement kiln clinker calcining heat " and " wet ammonia flue gas cleaning technology and the system thereof of desulphurization denitration simultaneously ", this dual mode is all separate process system, if simply with rich Combustion Technics and gas denitrifying technology in conjunction with system complex not only, equipment is many, construction area is large, investment and operating cost are all very high, and two independently system simply be combined and can not realize efficient effects of energy conservation and environmental protection.
Summary of the invention
The utility model purpose is to provide a kind of Industrial Stoves rich Combustion Technics and flue gas desulfurization and denitrification technology is combined, utilize on the one hand rich Combustion Technics to save the Industrial Stoves firing rate and solve requirement to ature of coal, improve the quality of Industrial Stoves grog, on the other hand, reduce NO in the Industrial Stoves discharging waste gas
XAnd SO
XContent, reach the country to various Industrial Stoves NO
XDischarge standard a kind of realizes the Industrial Stoves oxygen-enriched combustion-supporting system that combines with flue gas desulfurization and denitrification.
To achieve these goals, the utility model adopts following technical scheme:
The outlet of Industrial Stoves body tail flue gas is connected with the deduster import, also can be connected with the deduster outlet by waste heat boiler; The outlet of this deduster is connected with the gas approach of desulfurization and denitrification reaction tower, and the exhanst gas outlet of this desulfurization and denitrification reaction tower is connected with chimney, and this desulfurization and denitrification reaction tower bottom is provided with the ammonium salt pond, is provided with ammonium salt bottom it to export, and it is connected with the ammonium salt liquid-solid separation device.This desulfurization and denitrification reaction tower top is provided with the reducing agent import, and it is connected with SNCR denitrification reducing agent spraying atomizing device.Also be provided with the ozone import on this desulfurization and denitrification reaction tower, it is connected with ozone generating-device, and this ozone generating-device import is connected with an outlet of oxygen enrichment generating means.Another outlet of this oxygen enrichment generating means is connected with an import that mixes the wind matching device, should also be provided with hot-air inlets on mixed wind matching device, the outlet of this mixed wind matching device is connected with the combustion-supporting nozzle in being located at Industrial Stoves, makes oxygen enrichment enter Industrial Stoves and carries out oxygen-enriched combustion-supporting.
Above-mentioned oxygen enrichment generating means can have multiple, as all kinds of oxygen enrichment generating means such as Deep Cooling Method oxygen enrichment generating means, film oxygen enriching generating means, pressure swing adsorption method oxygen enrichment generating means.
Operation principle of the present utility model: adopt rich Combustion Technics at the Industrial Stoves combustion phases, improved on the one hand flame temperature and flame blackness, accelerate burning velocity, reduce fuel burning-point and tail-off time, lower coefficient of excess air, make fuel combustion more abundant, thereby reduced NO
XAnd SO
XGeneration, reached the purpose of energy-saving and emission-reduction.On the other hand, the oxygen enrichment of recycling concentration 40% ~ 90% produces ozone in ozone generating-device, and the desulfuring and denitrifying apparatus of coupling system end carries out denitration to flue gas, and front and back two cover system combinations have improved the efficient of Industrial Stoves desulphurization denitrations greatly.In flue gas desulfurization and denitrification device part, due to the NO in flue gas
XMainly accounted for more than 90% by NO() form, NO is insoluble in water, adopts ozone as oxidant, contacts the generation oxidation reaction with NO and can generate NO
2(its oxygenation efficiency is in 90% left and right), and the NO of high valence state
2Water soluble generates HNO
3, solvability improves greatly, simultaneously SO
2Also can be become SO by ozone oxidation
3Thereby make NO
2Can with SO
3Be absorbed simultaneously agent and absorb, ammoniacal liquor and NO
2Contact the generation ammonium nitrate that reacts, ammoniacal liquor and SO
3Contact the generation ammonium sulfate that reacts, reach the purpose of desulphurization denitration simultaneously.
The utility model compared with prior art advantage is as follows:
1, due to Industrial Stoves are adopted rich Combustion Technics and gas denitrifying technology simultaneously, so this system's fuel savings and energy, general synthesis energy saving improves output at 5%-30%, and has reduced NO in flue gas at 2%-30%
XAnd SO
XDischarging, NO
XConcentration of emission can drop to below 200mg/Nm3, reaches the discharging standards of denitrating flue gas.
2, because the Industrial Stoves rich Combustion Technics is being saved Industrial Stoves fuel, in the time of the raising product quality, the CO in the flue gas, CO have also been reduced
2, NO
X, SO
X, for example when Rich Oxygen Amount be combustion air volume 4% the time, CO, CO
2, NO
X, descend 71.4%, 22%, 54% respectively, clean fractional energy savings has reached 18.3%.In conjunction with the flue gas desulfurization and denitrification device of kiln tail, significantly improved the efficient of industrial furnace smoke desulphurization denitration again, its denitration efficiency is up to more than 90%.
3, the dust average rate of decrease is 90%, and dust removing effects is very obvious, and kiln exit gas pm emission dust concentration has reduced the final dusting of Industrial Stoves systems much smaller than 50mg/Nm3, has saved civil engineering and equipment cost with deduster.
4, because two cover technology merge aspect producing mutually at oxygen source, adopted common oxygen source device, made equipment still less, technique is simpler, reduces occupation area of equipment, saves investment and operating cost, approximately can save 10%.
5, the byproduct of desulphurization denitration acquisition is that ammonium nitrate and ammonium sulfate can be used as chemical fertilizer.
6, system is simple, the structure motion parts are less, so the maintenance of equipment amount is little.
7, the grog that effectively improves the cement kiln in Industrial Stoves burns till quality, and can improve finished cement 3 days, 28 days intensity.
Description of drawings
Fig. 1 is the flow process simplified schematic diagram of the utility model example 1.
Fig. 2 is the flow process simplified schematic diagram of the utility model example 2.
Fig. 3 is the flow process simplified schematic diagram of the utility model example 3.
In figure 1, the oxygen enrichment generating means, 2, mixed wind matching device, 3, the cement kiln kiln hood, 4, burner, 5, the cement rotary kiln body, 6, kiln tail predecomposition furnace, 7, electric cleaner, 8, ozone generating-device, 9, the desulfurization and denitrification reaction tower, 10, SNCR denitrification reducing agent atomization jetting device, 11, ammonium salt liquid-solid separation device, 12, chimney, 13, waste heat boiler, 14, furnace, 15 glass furnaces.
The specific embodiment
In a kind of simplified schematic diagram that realizes system's example 1 that the cement kiln oxygen-enriched combustion-supporting combines with flue gas desulfurization and denitrification shown in Figure 1, the cement rotary kiln body portion is provided with the cement kiln kiln hood, and the kiln tail is established the stove tail and separated in advance stove.This dore furnace is connected with the thermal medium entrance of preheater, this preheater is plural serial stage, the outlet of afterbody preheater is connected with the exhaust-heat boiler flue gas import, the exhaust-heat boiler flue gas outlet is connected with the deduster import, this deduster outlet is connected with the gas approach of desulfurization and denitrification reaction tower, and the exhanst gas outlet of this desulfurization and denitrification reaction tower is connected with chimney.This desulfurization and denitrification reaction tower bottom is provided with the ammonium salt pond, and its bottom is provided with the ammonium salt outlet, and it is connected with the ammonium salt liquid-solid separation device.This desulfurization and denitrification reaction tower top is provided with the reducing agent import, and it is connected with SNCR denitrification reducing agent spraying atomizing device.Also be provided with the ozone import on this desulfurization and denitrification reaction tower, it is connected with ozone generating-device, and this ozone generating-device import is connected with the outlet that the oxygen enrichment generating means is the film oxygen enriching generating means.Another outlet of this oxygen enrichment generating means is connected with an import that mixes the wind matching device, also is provided with hot-air inlets on this mixed wind matching device, the outlet of this mixed wind matching device be located at rotary kiln end and be connected with combustion-supporting nozzle in kiln tail dore furnace.
In a kind of simplified schematic diagram that realizes system's example 2 that the furnace oxygen-enriched combustion-supporting combines with flue gas desulfurization and denitrification shown in Figure 2, the outlet of furnace body tail flue gas is connected with the exhaust-heat boiler flue gas import, the exhaust-heat boiler flue gas outlet is connected with the deduster import, this deduster outlet is connected with the gas approach of desulfurization and denitrification reaction tower, and the exhanst gas outlet of this desulfurization and denitrification reaction tower is connected with chimney.This desulfurization and denitrification reaction tower bottom is provided with the ammonium salt pond, and its bottom is provided with the ammonium salt outlet, and it is connected with the ammonium salt liquid-solid separation device.This desulfurization and denitrification reaction tower top is provided with the reducing agent import, and it is connected with SNCR denitrification reducing agent spraying atomizing device.Also be provided with the ozone import on this desulfurization and denitrification reaction tower, it is connected with ozone generating-device, and this ozone generating-device import is connected with the outlet that the oxygen enrichment generating means is pressure swing adsorption method oxygen enrichment generating means.Another outlet of this oxygen enrichment generating means is connected with an import that mixes the wind matching device, also is provided with hot-air inlets on this mixed wind matching device, and the outlet of this mixed wind matching device is connected with combustion-supporting nozzle in being located at furnace.
In a kind of simplified schematic diagram that realizes system's example 3 that the glass furnace oxygen-enriched combustion-supporting combines with flue gas desulfurization and denitrification shown in Figure 3, the outlet of glass furnace body tail flue gas is connected with the exhaust-heat boiler flue gas import, the exhaust-heat boiler flue gas outlet is connected with the deduster import, this deduster outlet is connected with the gas approach of desulfurization and denitrification reaction tower, and the exhanst gas outlet of this desulfurization and denitrification reaction tower is connected with chimney.This desulfurization and denitrification reaction tower bottom is provided with the ammonium salt pond, and its bottom is provided with the ammonium salt outlet, and it is connected with the ammonium salt liquid-solid separation device.This desulfurization and denitrification reaction tower top is provided with the reducing agent import, and it is connected with SNCR denitrification reducing agent spraying atomizing device.Also be provided with the ozone import on this desulfurization and denitrification reaction tower, it is connected with ozone generating-device, and this ozone generating-device import is connected with the outlet that the oxygen enrichment generating means is Deep Cooling Method oxygen enrichment generating means.Another outlet of this oxygen enrichment generating means is connected with an import that mixes the wind matching device, also is provided with hot-air inlets on this mixed wind matching device, and the outlet of this mixed wind matching device is connected with combustion-supporting nozzle in being located at glass furnace.
Claims (4)
1. realize the Industrial Stoves oxygen-enriched combustion-supporting system that combines with flue gas desulfurization and denitrification for one kind, its Industrial Stoves body tail flue gas outlet is connected with the deduster import, it is characterized in that: this deduster outlet is connected with the gas approach of desulfurization and denitrification reaction tower, the exhanst gas outlet of this desulfurization and denitrification reaction tower is connected with chimney, this desulfurization and denitrification reaction tower bottom is provided with the ammonium salt pond, its bottom is provided with the ammonium salt outlet, this desulfurization and denitrification reaction tower top is provided with the reducing agent import, it is connected with SNCR denitrification reducing agent spraying atomizing device, also be provided with the ozone import on this desulfurization and denitrification reaction tower, it is connected with ozone generating-device, this ozone generating-device import is connected with an outlet of oxygen enrichment generating means, another outlet of this oxygen enrichment generating means is connected with an import that mixes the wind matching device, should also be provided with hot-air inlets on mixed wind matching device, the outlet of this mixed wind matching device is connected with the combustion-supporting nozzle in being located at Industrial Stoves.
2. a kind of Industrial Stoves oxygen-enriched combustion-supporting system that combines with flue gas desulfurization and denitrification of realizing according to claim 1, it is characterized in that: described oxygen enrichment generating means can be Deep Cooling Method oxygen enrichment generating means, film oxygen enriching generating means or pressure swing adsorption method oxygen enrichment generating means.
3. a kind of Industrial Stoves oxygen-enriched combustion-supporting system that combines with flue gas desulfurization and denitrification of realizing according to claim 1, is characterized in that: can be provided with waste heat boiler between described Industrial Stoves body tail flue gas outlet and deduster import.
4. a kind of Industrial Stoves oxygen-enriched combustion-supporting system that combines with flue gas desulfurization and denitrification of realizing according to claim 1, it is characterized in that: the ammonium salt outlet in ammonium salt pond, described desulfurization and denitrification reaction tower bottom is connected with the ammonium salt liquid-solid separation device.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200943904U CN203264541U (en) | 2013-03-01 | 2013-03-01 | System capable of combining oxygen-enriched combustion supporting with flue gas desulfurization and denitration for industrial kiln |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200943904U CN203264541U (en) | 2013-03-01 | 2013-03-01 | System capable of combining oxygen-enriched combustion supporting with flue gas desulfurization and denitration for industrial kiln |
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|---|---|
| CN203264541U true CN203264541U (en) | 2013-11-06 |
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|---|---|---|---|
| CN2013200943904U Expired - Fee Related CN203264541U (en) | 2013-03-01 | 2013-03-01 | System capable of combining oxygen-enriched combustion supporting with flue gas desulfurization and denitration for industrial kiln |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103170225A (en) * | 2013-03-01 | 2013-06-26 | 大连易世达新能源发展股份有限公司 | System for realizing combination of oxygen-enriched combustion assistance and flue gas desulfurization and denitrification of industrial kiln furnace |
| CN109224805A (en) * | 2018-10-17 | 2019-01-18 | 四川锐源能环科技有限公司 | A kind of ultra-clean exhaust system of fire coal |
-
2013
- 2013-03-01 CN CN2013200943904U patent/CN203264541U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103170225A (en) * | 2013-03-01 | 2013-06-26 | 大连易世达新能源发展股份有限公司 | System for realizing combination of oxygen-enriched combustion assistance and flue gas desulfurization and denitrification of industrial kiln furnace |
| CN109224805A (en) * | 2018-10-17 | 2019-01-18 | 四川锐源能环科技有限公司 | A kind of ultra-clean exhaust system of fire coal |
| CN109224805B (en) * | 2018-10-17 | 2024-02-20 | 四川锐源能环科技有限公司 | Coal-fired ultra-clean emission system |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: Floor 20, block B, No. 32a, Torch Road, high tech Industrial Park, Dalian, Liaoning Province, 116000 Patentee after: Lida Group Co., Ltd Address before: 116023, B building, No. 32, Torch Road, Dalian hi tech Zone, Liaoning, 18 Patentee before: DALIAN EAST NEW ENERGY DEVELOPMENT Co.,Ltd. |
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| CP03 | Change of name, title or address | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131106 Termination date: 20210301 |
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| CF01 | Termination of patent right due to non-payment of annual fee |