CN102614761A - Glass coating waste gas treatment dry energy-saving process - Google Patents
Glass coating waste gas treatment dry energy-saving process Download PDFInfo
- Publication number
- CN102614761A CN102614761A CN2012101112039A CN201210111203A CN102614761A CN 102614761 A CN102614761 A CN 102614761A CN 2012101112039 A CN2012101112039 A CN 2012101112039A CN 201210111203 A CN201210111203 A CN 201210111203A CN 102614761 A CN102614761 A CN 102614761A
- Authority
- CN
- China
- Prior art keywords
- waste gas
- dust
- coating film
- glass
- spray tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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- 239000002912 waste gas Substances 0.000 title claims abstract description 25
- 238000000576 coating method Methods 0.000 title claims abstract description 21
- 239000011521 glass Substances 0.000 title claims abstract description 21
- 239000011248 coating agent Substances 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 title claims abstract description 17
- 239000000428 dust Substances 0.000 claims abstract description 30
- 238000005516 engineering process Methods 0.000 claims abstract description 28
- 238000001816 cooling Methods 0.000 claims abstract description 17
- 239000007921 spray Substances 0.000 claims abstract description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 27
- 239000003546 flue gas Substances 0.000 claims description 20
- 239000003795 chemical substances by application Substances 0.000 claims description 12
- 239000007789 gas Substances 0.000 claims description 8
- 239000010922 glass waste Substances 0.000 claims description 6
- 239000004744 fabric Substances 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 3
- 210000002356 Skeleton Anatomy 0.000 claims 1
- 229910000831 Steel Inorganic materials 0.000 claims 1
- 239000002253 acid Substances 0.000 claims 1
- 238000006386 neutralization reaction Methods 0.000 claims 1
- 239000010959 steel Substances 0.000 claims 1
- 238000006477 desulfuration reaction Methods 0.000 abstract description 11
- 230000003009 desulfurizing Effects 0.000 abstract description 9
- 238000002485 combustion reaction Methods 0.000 abstract 2
- 239000003153 chemical reaction reagent Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 abstract 1
- 239000003344 environmental pollutant Substances 0.000 abstract 1
- 239000002957 persistent organic pollutant Substances 0.000 abstract 1
- 231100000719 pollutant Toxicity 0.000 abstract 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 238000000605 extraction Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005453 pelletization Methods 0.000 description 2
- 230000002588 toxic Effects 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000002349 favourable Effects 0.000 description 1
- 239000005357 flat glass Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000002045 lasting Effects 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 230000001473 noxious Effects 0.000 description 1
- 230000000505 pernicious Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Abstract
The invention discloses a process for controlling glass coating waste gas through dry dust removal and desulfurization technology. The process comprises a combustion system, a cooling system, a dust removal system, a desulphurization system, a dust collection system, a secondary high-efficiency dust removal system and a reagent return system; all the systems are sequentially connected and combined with practicality, can remove organic pollutant in glass coating waste gas through combustion, and perform desulfurization and dust removal treatment on the waste gas after cooling, and finally ensure that the waste gas meets the discharge standard. The process has the key point that all units in the process are organically combined, especially, a novel turbulence spray tower mode is adopted for desulfurization, the pollutant is ensured to meet the discharge standard, secondary pollution can not be caused, the process has the advantages of engineering practicability, good control effect, fully automatic operation, reduced investment and the like, and has a wide market prospect.
Description
Technical field
New technology of the present invention is the novel process that a cover utilization dry method power-saving technology is handled online coating film on glass waste gas.
Background technology
The waste gas main component that online coating film on glass technology produces is organic fuel gas, flue dust, sulfur-containing smoke gas etc., and the improvement to this type pernicious gas is main with wet method in the world.Domestic waiting developed, and has certain difficulty and problem with high investment on the treatment technology.Multi-stage processing equipment is connected and technological design is very big difficult point, especially a wet processing process, and deacidification efficiency is low, brings the secondary pollution and the processing of water, increases a lot of difficulties and trouble.At present; The coating process that many sized glasses enterprise arranged in various degree exist exhaust emission discharging exceed standard (national standard); Country has issued plate glass technology waste gas discharge standard; But formulate as yet for coating film on glass technology waste gas discharge index relevant criterion, more at present glass industry waste gas standards wait perfect, and the coating film on glass waste gas pollution control and treatment is badly in need of more specialty, the more innovative technology appearance of standard, higher Governance Ability.
Can be used as the glass stove dedusting of the routine of reference, the technology that desulfurization is mainly adopted is wet dedusting, sulfur removal technology: mainly the advanced waste heat boiler of high-temperature flue gas (or cooler) is cooled off, when flue-gas temperature is lower than 250 ℃, flue gas is sent into high-efficient desulfation dust-extraction device and carry out desulfurization and dedusting and handle by air-introduced machine.Flue gas contacts with deacidification agent from the cleaning solution circulatory system in high-efficient desulfation dust-extraction device; Under the chemistry of a series of complicacies, physical action; Sulfur in smoke is washed liquid and absorbs, and the flue dust aggegation sedimentation in the flue gas simultaneously and be washed liquid and take away reaches the purpose of desulfurization and dedusting.Through flue gas after being purified, in high-efficient desulfation dust-extraction device, effectively dewater, the flue gas after the dehydration is effluxed by chimney stack.
The waste gas that coating film on glass produces is different from conventional glass stove flue gas, except that containing conventional glass stove smoke components, with the used film formulation composition of coating process much relations is arranged; Exhaust gas properties is main with organic exhaust gas; The higher suitable burning disposal of concentration also contains heavy metal particles, dust etc. simultaneously.So the present invention is combining to develop the dry method energy saving technique of innovative practical coating film on glass waste gas pollution control and treatment on the conventional glass stove flue gas managing technique basis.
Summary of the invention
The purpose of the present invention's technology is to satisfy the needs of coating film on glass waste gas pollution control and treatment, and the invention of glass plated film waste gas organic exhaust gas wet method sulphur removing and dust removing technology is dry method energy-saving desulfuration dust collecting process, provides a cover the complete efficient improvement technology that can be applicable to the practical applications scale.
For realizing above-mentioned purpose, the technology path that the present invention adopts is: a whole set of technology is made up of CIU, cooling system, dust pelletizing system, desulfurization dewatering system.Wherein CIU is made up of incinerator and built-in burner, and cooling system is made up of air blast cooling cooler and circulating water cooling system, and dust pelletizing system is made up of sack cleaner, and desulphurization system is made up of new type power ripple spray tower.Waste gas gets in the exhaust treatment system through air-introduced machine; Waste gas burns harmless treatment through incinerator to reluctant organic exhaust gas earlier; Get into air-cooled cooler through the waste gas after burning then and lower the temperature, waste gas gets into sack cleaner again and carries out dedusting, and waste gas gets into the dynamic wave spray tower more then and carries out desulfurization; Get into the waste gas of high-efficiency dust remover after at last and carry out dedusting, finally discharge through chimney by the 2# blower fan to desulfurization.
This invention technology mainly is made up of following apparatus and process: air-introduced machine (1), incinerator (2), wind cooling temperature lowering device (3), sack cleaner (4), turbulent flow spray tower (5), high-efficiency dust remover (6), dust compartment (7), backflow blower fan (8), exhaust blower (9), chimney (10).
Technology of the present invention has following advantage: 1. can use as the engineering large-scale promotion, realize commercialized running; 2. filled up the blank of coating film on glass waste gas dry treatment, perfect glass industry waste gas dry treatment technology; 3. dry treatment does not have problem of secondary pollution, and treatment cost is reduced, and governance process is energy-conserving and environment-protective more; 4. the dry treatment reaction is more abundant, and desulfuration efficiency improves; 5. technology is workable, has realized full-automatic operation, is that a cover is efficient, science, reasonable, lasting waste gas pollution control and treatment system, has favorable social and economic benefits.
Accompanying drawing and description of drawings
Fig. 1 is a coating film on glass emission control technology sketch map.
The specific embodiment
Below in conjunction with accompanying drawing patent of the present invention is done further explanation.
Plated film can produce a large amount of toxic and harmfuls and material, and these toxic and harmfuls get into incinerator through air-introduced machine.Through 800 ℃ high temperature incineration, noxious material burns the generation chemical reaction and makes inorganicization of organic exhaust gas organic exhaust gas under this high temperature, produce a large amount of sour gas and dust characteristic oxide in incinerator.
The flue gas of waste gas after incinerator burns makes flue-gas temperature be lower than the load temperature of deduster cloth bag by wild air cooling in the wind cooling temperature lowering device between 400-600 ℃.Wild wind is squeezed into the wind cooling temperature lowering device by axial flow blower around from the scene, in the wind cooling temperature lowering device with high temperature incineration after flue gas carry out heat exchange.
Flue gas in the cloth bag load temperature in deduster under rational filtration velocity through the cloth bag filtration, the dust in flue gas composition filtered be trapped in the dust collector ash hopper.
Dustless flue gas gets into the turbulent flow spray tower, and oversaturated deacidification agent gets in the tower body with solid-state attritive powder shape in the tower, and deacidification agent fully contacts with sour gas and absorbs sour gas simultaneously.
Flue gas after being purified also contains a spot of deacidification agent, carries out further dust removal process through high-efficiency dust remover again, and clean flue gas and a spot of deacidification agent are separated, and flue gas after being purified is discharged through chimney by exhaust blower.The deacidification agent of being separated by high-efficiency dust remover simultaneously gets into dust compartment, and the power that relies on the backflow blower fan to provide is back to remaining deacidification agent and fully contacts with sour gas once more in the turbulent flow spray tower and absorbs sour gas simultaneously.
Claims (5)
1. technology of using the dry method dust desulfur technology to administer coating film on glass waste gas; It is characterized in that: the waste gas that mainly comprises air-introduced machine (1), incinerator (2), wind cooling temperature lowering device (3), sack cleaner (4), turbulent flow spray tower (5), high-efficiency dust remover (6), dust compartment (7), backflow blower fan (8), exhaust blower (9), the generation of chimney (10) coating film on glass is delivered to fully burning of incinerator (2) through air-introduced machine (1); Waste gas after the burning gets into wind cooling temperature lowering device (3) and cools; Entering turbulent flow spray tower (5) carried out neutralization reaction after cooling back flue gas entering sack cleaner (4) carried out dust removal process; Flue gas after being purified is again through high-efficiency dust remover (6) dedusting; Again the deacidification agent of collecting is imported dust compartment (7); The power that utilizes backflow blower fan (8) to provide again is back to turbulent flow spray tower (5) with the deacidification agent in the dust compartment (7) makes remaining deacidification agent continue to react with acid waste gas, and the waste gas after handling at last is by exhaust blower (9) suction chimney (10) qualified discharge.
2. coating film on glass emission control technology according to claim 1 is characterized in that: air-introduced machine (1) carries out pressurized treatments to plated film waste gas, and exhaust blower (9) provides negative pressure to previous process equipment.
3. coating film on glass emission control technology according to claim 1 is characterized in that: wind cooling temperature lowering device (3) adopts indirect wind cooling temperature lowering mode, also comprises the wind cooling temperature lowering system.
4. coating film on glass emission control technology according to claim 1 is characterized in that: sack cleaner (4) comprises container body of steel plate, cage skeleton, filter cloth bag and pulse dust cleaning compressed air blowback system.
5. coating film on glass emission control technology according to claim 1; It is characterized in that: turbulent flow spray tower (5) adopts turbulent flow spray tower technology; Comprise sprayer unit, the deacidification agent circulatory system, wherein the deacidification agent circulatory system is made up of high-efficiency dust remover (6), dust compartment (7), backflow blower fan (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101112039A CN102614761A (en) | 2012-04-17 | 2012-04-17 | Glass coating waste gas treatment dry energy-saving process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101112039A CN102614761A (en) | 2012-04-17 | 2012-04-17 | Glass coating waste gas treatment dry energy-saving process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102614761A true CN102614761A (en) | 2012-08-01 |
Family
ID=46555178
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012101112039A Pending CN102614761A (en) | 2012-04-17 | 2012-04-17 | Glass coating waste gas treatment dry energy-saving process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102614761A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104841263A (en) * | 2015-06-02 | 2015-08-19 | 刘启杰 | Glass fiber furnace kiln waste gas desulfurization device with turbo-charging turbulator and process |
| CN108119904A (en) * | 2017-12-15 | 2018-06-05 | 长兴旗滨玻璃有限公司 | A kind of online solar control coated glass exhaust gas processing device and its treatment process |
| CN112933905A (en) * | 2021-01-29 | 2021-06-11 | 乌海宝杰新能源材料有限公司 | Efficient and energy-saving graphitized tail gas treatment system and treatment process thereof |
Citations (5)
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|---|---|---|---|---|
| JP2002058937A (en) * | 2000-08-18 | 2002-02-26 | Ishikawajima Harima Heavy Ind Co Ltd | Method for controlling pressure drop of bag filter |
| CN1425491A (en) * | 2002-12-09 | 2003-06-25 | 武汉凯迪电力股份有限公司 | Composite Circulation fluidized dry desulfurization process for flue gas and desalfurizing reaction tower |
| CN1488426A (en) * | 2003-08-15 | 2004-04-14 | 武汉凯迪电力股份有限公司 | Dry-process flue gas desulfurizing method using combined gas jet |
| CN101377386A (en) * | 2008-09-25 | 2009-03-04 | 中金兴环（北京）科技有限公司 | Metal smelting flue gas purification method |
| KR100949037B1 (en) * | 2009-10-12 | 2010-03-24 | (주)명성환경 | Eliminating apparatus of effluent gas comes from an organic waste |
-
2012
- 2012-04-17 CN CN2012101112039A patent/CN102614761A/en active Pending
Patent Citations (5)
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|---|---|---|---|---|
| JP2002058937A (en) * | 2000-08-18 | 2002-02-26 | Ishikawajima Harima Heavy Ind Co Ltd | Method for controlling pressure drop of bag filter |
| CN1425491A (en) * | 2002-12-09 | 2003-06-25 | 武汉凯迪电力股份有限公司 | Composite Circulation fluidized dry desulfurization process for flue gas and desalfurizing reaction tower |
| CN1488426A (en) * | 2003-08-15 | 2004-04-14 | 武汉凯迪电力股份有限公司 | Dry-process flue gas desulfurizing method using combined gas jet |
| CN101377386A (en) * | 2008-09-25 | 2009-03-04 | 中金兴环（北京）科技有限公司 | Metal smelting flue gas purification method |
| KR100949037B1 (en) * | 2009-10-12 | 2010-03-24 | (주)명성환경 | Eliminating apparatus of effluent gas comes from an organic waste |
Non-Patent Citations (1)
| Title |
|---|
| 杨福峰: "干法脱硫新工艺", 《环境科技》 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104841263A (en) * | 2015-06-02 | 2015-08-19 | 刘启杰 | Glass fiber furnace kiln waste gas desulfurization device with turbo-charging turbulator and process |
| CN108119904A (en) * | 2017-12-15 | 2018-06-05 | 长兴旗滨玻璃有限公司 | A kind of online solar control coated glass exhaust gas processing device and its treatment process |
| CN108119904B (en) * | 2017-12-15 | 2019-10-29 | 长兴旗滨玻璃有限公司 | A kind of online solar control coated glass exhaust gas processing device and its treatment process |
| CN112933905A (en) * | 2021-01-29 | 2021-06-11 | 乌海宝杰新能源材料有限公司 | Efficient and energy-saving graphitized tail gas treatment system and treatment process thereof |
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| PB01 | Publication | ||
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| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
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Application publication date: 20120801 |