CN105879546A - Technological process for treatment of flue gas - Google Patents

Technological process for treatment of flue gas Download PDF

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Publication number
CN105879546A
CN105879546A CN201610304416.1A CN201610304416A CN105879546A CN 105879546 A CN105879546 A CN 105879546A CN 201610304416 A CN201610304416 A CN 201610304416A CN 105879546 A CN105879546 A CN 105879546A
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CN
China
Prior art keywords
flue gas
fume
treatment
absorption
spray
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
Application number
CN201610304416.1A
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Chinese (zh)
Inventor
陈来福
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Chizhou Nature Environmental Protection Engineering Co Ltd
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Chizhou Nature Environmental Protection Engineering Co Ltd
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Publication date
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Priority to CN201610304416.1A priority Critical patent/CN105879546A/en
Publication of CN105879546A publication Critical patent/CN105879546A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D50/00Combinations of methods or devices for separating particles from gases or vapours
    • B01D50/10Combinations of devices covered by groups B01D45/00, B01D46/00 and B01D47/00
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1425Regeneration of liquid absorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2252/00Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/10Inorganic absorbents
    • B01D2252/103Water

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention relates to a technological process for the treatment of flue gas, comprising the following steps: absorbing the flue gas at an entry by spraying, dehydrating and dedusting the flue gas, removing adhesive substances, filtering dust droplets, cooling and condensing the flue gas, demisting and deaerating the flue gas, and discharging the flue gas out of a discharge outlet. After the flue gas is absorbed by spraying, sewage which is formed by absorbing pollution factors in the flue gas needs further treatment; a technological sub-process of water treatment forms a circulation; and pigments and organic harmful gas molecules in water are removed continuously in the circulation. The technological process for the treatment of the flue gas, provided by the invention, has the comprehensive functions of removing dust, smoke, mist and vapor as the pollution factors are subjected to a technological design of a multi-stage treatment in a classified and graded manner, and the sufficient treatment of the flue gas discharged in industry is realized.

Description

A kind of fume processing technological flow
Technical field
The present invention relates to environment-friendly treating process flow process field, particularly relate to a kind of fume processing technological flow.
Background technology
At present atmospheric pollution is very serious, and industrial fumes flue gas is one of important polluter, essentially from two kinds by way of: burn and dry dry;Increase chimney height and be not solution problem but escape problem, so must before discharge fume fully be processed.Various Industrial Boiler such as such as power plant etc., although large-sized boiler has all carried out desulphurization denitration process, but these process in technique most in order to not allow the pipelines such as chimney be corroded, GGH system is used to have a mind to improve the temperature of discharge, result discharge time create substantial amounts of haze, so must also carry out advanced treating or increase process technique accordingly;The such as drying of the industry such as wood-based plate and glass fibre is dried, and produces the organic harmful gas of substantial amounts of high temperature and aqueous vapor, although part factory have also been made some and processes, but the result processed is substantially less than position, and especially autumn and winter season is still that white cigarette dances in the air.
Summary of the invention
For the problem of shortcomings and deficiencies in prior art, the present invention proposes a kind of fume processing technological flow, each pollution factor is classified classification multistage treatment process design, have dedusting, smoke abatement, except mist and deaeration comprehensive function, it is achieved that to the abundant process discharging fume in industry.
The technical solution adopted for the present invention to solve the technical problems is:
A kind of fume processing technological flow, its technological process is: fume import is to spray-absorption, then is dehydrated dedusting, removes stickum, and micronic dust droplet filters, cooling condensation, except mist deaeration, is finally discharged by floss hole.
Further, described fume import is provided with emergent floss hole to spray-absorption flow process.
Further, described fume is after spray-absorption, absorb the sewage that in fume, pollution factor is formed need to be for further processing, its water processes sub-technological process: the most heavy process, grid initial filter, deposition filter, air floatation machine processes, pond in entrance, divides the most again two-way: clear water reserviors are directly arrived on a road, enters the circulation of next water;Another road: carry out desolventing technology, quartz sand filtration adsorbs, activated carbon Filtration Adsorption, then to clear water reserviors.
Further, the water of described clear water reserviors returns spray-absorption and forms circulation.
There is advantages that the present invention uses water to absorb the pollution factor in fume, to sewage purified treatment again, make water recycle, saved and used water.The present invention is also classified classification multistage treatment process design to each pollution factor, have dedusting, smoke abatement, except mist and deaeration comprehensive function, it is possible to the pollution to industrial discharge fume reaches sufficient treatment effect.
Accompanying drawing explanation
Fig. 1 is present invention process schematic flow sheet.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention is expanded on further.Should be understood that these embodiments are merely to illustrate the present invention rather than limit the scope of the present invention.In addition, it is to be understood that after having read the content that the present invention lectures, the present invention can be made various changes or modifications by those skilled in the art, and these equivalent form of values fall within the application appended claims limited range equally.
As it can be seen, a kind of fume processing technological flow, its technological process is: fume import is to spray-absorption, then is dehydrated dedusting, removes stickum, and micronic dust droplet filters, cooling condensation, except mist deaeration, is finally discharged by floss hole.
Described fume import is provided with emergent floss hole to spray-absorption flow process, prevents the interrupt processing because of equipment fault in follow-up flow process, untreated fume can carry out emergent discharge, it is to avoid cause the impact produced.
Described fume is after spray-absorption, absorb the sewage that in fume, pollution factor is formed need to be for further processing, its water processes sub-technological process: the most heavy process, grid initial filter, deposition filter, air floatation machine processes, pond in entrance, divide the most again two-way: clear water reserviors are directly arrived on a road, enter the circulation of next water;Another road: carry out desolventing technology, quartz sand filtration adsorbs, activated carbon Filtration Adsorption, then to clear water reserviors.
The water of described clear water reserviors returns spray-absorption and forms circulation.
Cause pollute produce because have: solid particulate matter, flue gas, steam and high temperature;Generating the biggest material of viscosity after the cooling of some flue gas, the essence process that the present invention processes is first by during in the fume of industrial discharge, pollution factor transfers to recirculated water, makes gas qualified discharge, then processes recirculated water.
Concrete, described spray-absorption is to be sprayed flue gas by corresponding shower respectively by multiple stage high-pressure hydraulic pump, drenches weighting solids particulate matter, solution absorption flue gas, cooled flue gas;Dehydration dedusting is formed by organizing cyclonic separation unit more, utilizes centrifugal force weight in wet base particulate matter and drop to be separated from flue gas;Remove stickum to be made up of a series of flaps, capture those stickums formed because of cooling, and allow it automatically wander, because one Processing Equipment under the influence of the meeting of these stickums;Micronic dust droplet filters and is made up of finer drainage screen and self-stripping unit, after former roads PROCESS FOR TREATMENT, still has some micronic dusts and droplet;Cooling condensation is made up of numerous cooling tubes, and pending flue gas, at cooling Bottomhole pressure, carries out heat exchange by tube wall with external environment and cools down;Because flue-gas temperature at this moment is the highest, absolute humidity is big, especially autumn and winter season, if emit necessarily be cooled to mist and dissolve those not processed fall trace harmful gases;Except mist deaeration is made up of the filter cloth bag of super large surface area and densification, filter superfine little mist.Processing through one flow process, the pollutant in flue gas are eliminated substantially, and gas temperature is also close to ambient temperature, can not only qualified discharge, nor haze can be formed.
Fume is after spray-absorption, and during in fume, pollution factor transfers to recirculated water, the most heavy process is to utilize preliminary sedimentation tank that the most heavier material is carried out precipitation process;Grid initial filter is to utilize grid that material lighter relatively greatly is carried out primary filter process;Deposition filter is to precipitate less deposit and less suspended material and filtration treatment;It is that tiny float is carried out dissolved air flotation process that air floatation machine processes;Pond in water body entrance after process.
Owing to discharge is bigger, the moisture two-way in middle pond, a road is directly arrived clear water reserviors, is entered the circulation of next water;Another road carries out the bleaching that decolours to water body;Quartz sand filtration is to adsorb small float and filtration treatment;Activated carbon adsorption is that the organic gas molecule being dissolved in water is carried out adsorption treatment, and the clear water after process enters in clear water reserviors, and such purpose is to remove the pigment in water and organic harmful gas molecule, say, that process in water circulates.
A kind of fume processing technological flow of the present invention, each pollution factor is classified classification multistage treatment process design, have dedusting, smoke abatement, except mist and deaeration comprehensive function, it is possible to the pollution to industrial discharge fume reaches sufficient treatment effect.

Claims (4)

1. a fume processing technological flow, it is characterised in that technological process is: fume import is to spray-absorption, then is dehydrated dedusting, removes stickum, and micronic dust droplet filters, cooling condensation, except mist deaeration, is finally discharged by floss hole.
A kind of fume processing technological flow the most according to claim 1, it is characterised in that: described fume import to spray-absorption flow process is provided with emergent floss hole.
A kind of fume processing technological flow the most according to claim 1, it is characterized in that: described fume is after spray-absorption, absorb the sewage that in fume, pollution factor is formed need to be for further processing, its water processes sub-technological process: the most heavy process, grid initial filter, deposition filter, air floatation machine processes, pond in entrance, divides the most again two-way: clear water reserviors are directly arrived on a road, enters the circulation of next water;Another road: carry out desolventing technology, quartz sand filtration adsorbs, activated carbon Filtration Adsorption, then to clear water reserviors.
A kind of fume processing technological flow the most according to claim 3, it is characterised in that: the water of described clear water reserviors returns spray-absorption and forms circulation.
CN201610304416.1A 2016-05-09 2016-05-09 Technological process for treatment of flue gas Pending CN105879546A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610304416.1A CN105879546A (en) 2016-05-09 2016-05-09 Technological process for treatment of flue gas

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Application Number Priority Date Filing Date Title
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106906016A (en) * 2017-03-31 2017-06-30 山西都宝新能源发展研究院 A kind of energy-efficient pretreatment process method for the gas that generates electricity
CN108421373A (en) * 2017-11-01 2018-08-21 海盐哈特惠机械五金制品有限公司 A kind of vent gas treatment discharge technology
CN109589725A (en) * 2019-01-25 2019-04-09 内蒙古阜丰生物科技有限公司 A kind of flue gas processing method and processing system
CN112691495A (en) * 2021-01-29 2021-04-23 浙江金潮实业有限公司 Method for treating waste gas generated in synthetic leather production process

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003088729A (en) * 2001-09-19 2003-03-25 Shingo Kaneko Method for removing dioxins by activated carbon adsorption and removal apparatus therefor
WO2007035169A1 (en) * 2005-09-21 2007-03-29 Metso Power Ab A method for the cleaning of flue gases and the treatment of ash from the combustion of refuse
CN104548842A (en) * 2014-12-23 2015-04-29 哈尔滨金大环境工程有限公司 Cyclone diffusion type smoke prevention and dust control device and smoke prevention and dust control method
CN204723902U (en) * 2015-05-13 2015-10-28 常州禹豪防水科技有限公司 Pitch emission-control equipment
CN105169863A (en) * 2015-08-17 2015-12-23 杭州科瑞特环境技术有限公司 Integrated treating apparatus and treating process for exhaust gas of setting machine used in dyeing and finishing industry
CN105289132A (en) * 2015-11-19 2016-02-03 苏州韵蓝环保科技有限公司 Modularized exhaust-gas treatment device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003088729A (en) * 2001-09-19 2003-03-25 Shingo Kaneko Method for removing dioxins by activated carbon adsorption and removal apparatus therefor
WO2007035169A1 (en) * 2005-09-21 2007-03-29 Metso Power Ab A method for the cleaning of flue gases and the treatment of ash from the combustion of refuse
CN104548842A (en) * 2014-12-23 2015-04-29 哈尔滨金大环境工程有限公司 Cyclone diffusion type smoke prevention and dust control device and smoke prevention and dust control method
CN204723902U (en) * 2015-05-13 2015-10-28 常州禹豪防水科技有限公司 Pitch emission-control equipment
CN105169863A (en) * 2015-08-17 2015-12-23 杭州科瑞特环境技术有限公司 Integrated treating apparatus and treating process for exhaust gas of setting machine used in dyeing and finishing industry
CN105289132A (en) * 2015-11-19 2016-02-03 苏州韵蓝环保科技有限公司 Modularized exhaust-gas treatment device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106906016A (en) * 2017-03-31 2017-06-30 山西都宝新能源发展研究院 A kind of energy-efficient pretreatment process method for the gas that generates electricity
CN108421373A (en) * 2017-11-01 2018-08-21 海盐哈特惠机械五金制品有限公司 A kind of vent gas treatment discharge technology
CN109589725A (en) * 2019-01-25 2019-04-09 内蒙古阜丰生物科技有限公司 A kind of flue gas processing method and processing system
CN112691495A (en) * 2021-01-29 2021-04-23 浙江金潮实业有限公司 Method for treating waste gas generated in synthetic leather production process
CN112691495B (en) * 2021-01-29 2022-06-24 浙江金潮实业有限公司 Method for treating waste gas generated in synthetic leather production process

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Application publication date: 20160824