CN105597527B - The administering method of waste gas in a kind of production process of viscose fiber - Google Patents

The administering method of waste gas in a kind of production process of viscose fiber Download PDF

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Publication number
CN105597527B
CN105597527B CN201510952244.4A CN201510952244A CN105597527B CN 105597527 B CN105597527 B CN 105597527B CN 201510952244 A CN201510952244 A CN 201510952244A CN 105597527 B CN105597527 B CN 105597527B
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spray column
waste gas
alkali spray
level
alkali
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CN105597527A (en
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张仁友
张玉剑
黄盛国
易启永
陈轶
刘永洋
陈志梁
郝军
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Yibin Haisite Fiber Co Ltd
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Yibin Haisite Fiber Co Ltd
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    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8603Removing sulfur compounds
    • B01D53/8612Hydrogen sulfide
    • 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
    • B01D53/32Separation 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 electrical effects other than those provided for in group B01D61/00
    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/38Removing components of undefined structure
    • B01D53/44Organic components
    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/50Sulfur oxides
    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/52Hydrogen sulfide
    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8603Removing sulfur compounds
    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8678Removing components of undefined structure
    • B01D53/8687Organic components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/10Oxidants
    • B01D2251/104Ozone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/30Alkali metal compounds
    • B01D2251/302Alkali metal compounds of lithium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/30Sulfur compounds
    • B01D2257/304Hydrogen sulfide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/30Sulfur compounds
    • B01D2257/308Carbonoxysulfide COS
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s

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

Abstract

The present invention relates to a kind of administering method of waste gas in production process of viscose fiber, belongs to textile industry waste gas pollution control and treatment technical field.The present invention is handled caused waste gas in production process of viscose fiber after the washing of one-level alkali spray column into low-temperature plasma device, catalytic oxidation treatment is carried out to waste gas subsequently into catalytic oxidation treatment bed, two level alkali spray column is introduced into finally by fiberglass centrifugal blower and tiny molecule remaining in waste gas is absorbed.By said process, carbon disulfide and hydrogen sulfide waste gas can be resolved into CO2、H2O、N2Etc. innoxious material, qualified discharge is carried out.

Description

The administering method of waste gas in a kind of production process of viscose fiber
Technical field
The present invention relates to a kind of administering method of waste gas, it is more particularly related to which a kind of viscose rayon produced The administering method of waste gas in journey, belong to textile industry waste gas pollution control and treatment technical field.
Background technology
Caused waste gas is mainly CS in production process of viscose fiber at present2And H2S gases, these waste gas are to pass through glass Glass steel centrifugal blower passes through after extracting out to be handled by alkali spray or is discharged again after other are handled, but treatment effect and is paid no attention to Think.
State Intellectual Property Office discloses a Publication No. CN103331083A in 2013.10.2, and entitled " one kind is viscous The invention of the recovery process of carbon disulfide in glue fiber production ", carbon disulfide in being produced the invention provides a kind of viscose rayon Recovery process.It is characterized in that:The sulphur that caused carbon disulfide waste gas is gone in removing exhaust gas through alkali spray in viscose rayon production After changing hydrogen, then pass through following processing step recovery carbon disulfide:A) by the use of white oil as absorbent, the curing in waste gas is absorbed Carbon, the carbon disulfide rich solution after absorption saturation is cooled to 15 ~ 35 DEG C;B the carbon disulfide rich solution after saturation) is absorbed by pump to enter Enter Analytic Tower, after liquid distribution trough, be heated to 150 DEG C ~ 170 DEG C, the isolated carbon disulfide gas of liquid boiling and lean solution; C the carbon disulfide that) carbon disulfide gas is condensed, gas-liquid separation recovery condenses out.The recovery process absorptivity of the present invention is high, Investment and operating cost are low.
Although above-mentioned technical proposal can reclaim carbon disulfide, finally still there is discharge, CO can not be resolved into2、H2O、N2 Etc. innoxious material.
The content of the invention
Present invention seek to address that caused waste gas is decomposed into innocuous gas during viscose rayon can not be produced in the prior art The problem of, there is provided the administering method of waste gas in a kind of production process of viscose fiber, two caused by during can viscose rayon be produced Nitric sulfid and hydrogen sulfide gas resolve into innocuous gas, qualified discharge.
In order to realize foregoing invention purpose, its specific technical scheme is as follows:
The administering method of waste gas in a kind of production process of viscose fiber, it is characterised in that:Including following methods step:
A, one-level alkali spray pretreatment
Alkali spray column is connected, forms one-level alkali spray column, carbon disulfide and hydrogen sulfide waste gas by one-level alkali spray column, By interception, collision and the absorption of alkali lye spray and filler, it is volatilizable to remove hydrogen sulfide, a small amount of carbon disulfide and dissolubility Organic compound;
B, reaction is decomposed
Surge tank water removal will be first passed through by the pretreated waste gas of one-level spray column in step A, then pass through pipeline To low-temperature plasma device, the pollutant in waste gas is decomposed, is changed into small molecules fragments;
C, catalysis oxidation
By step B by low-temperature plasma device waste gas be delivered to catalytic oxidation treatment bed reaction, oxidation Decomposition into Pollution-free material;
D, two level alkali spray post processing
Alkali spray column is connected, two level alkali spray column is formed, waste gas of the step C after catalytic oxidation decomposes is led to Cross fiberglass centrifugal blower and introduce described two level alkali spray column, post-processed, gas qualified discharge, absorbing liquid recovery profit With.
The air quantity of waste gas of the present invention is the m of 5-10 ten thousand3/ h, the one-level alkali spray column are connected for 2-6 platform alkali spray column, The two level alkali spray column is connected for 2-6 platform alkali spray column.
The specified tolerance of low-temperature plasma device of the present invention is the m of 5-10 ten thousand3/ h, peak power 50-80Kw, input Voltage 380v.
When the air quantity of the waste gas is 50,000 m3During/h, the one-level alkali spray column is that 2 alkali spray columns are connected, described two Level alkali spray column is that 2 alkali spray columns are connected, and the specification of every spray column is 3600 × 12000mm of Φ.
The spray flow 120m of above-mentioned every alkali spray column3/ h, lift 20m, power 11kw, drug concentration 8-10%.
When the air quantity of the waste gas is 100,000 m3During/h, the one-level alkali spray column is that 6 alkali spray columns are connected, described two Level alkali spray column is that 6 alkali spray columns are connected, and the specification of every spray column is 2600 × 7600mm of Φ.
The spray flow 55m of above-mentioned every alkali spray column3/ h, lift 25m, power 11kw, drug concentration 8-10%.
The advantageous effects that the present invention is brought:
1st, the present invention solve viscose rayon can not be produced in the prior art in caused waste gas be decomposed into innocuous gas The problem of.Caused waste gas in production process of viscose fiber is entered low temperature etc. by the present invention after the washing of one-level alkali spray column Ion body device is handled, and catalytic oxidation treatment is carried out to waste gas subsequently into catalytic oxidation treatment bed, finally by glass Steel centrifugal blower is introduced into two level alkali spray column and tiny molecule remaining in waste gas is absorbed.By said process, can incite somebody to action Carbon disulfide and hydrogen sulfide waste gas resolve into CO2、H2O、N2Etc. innoxious material, qualified discharge is carried out.
2nd, on the spot/teletransmission control can be achieved in all power-equipments of the present invention, and reference PLC is core control part.Part Power-equipment can realize interlocked control by PLC.
3rd, this method can effectively remove caused CS in production process of viscose fiber2And H2S, make CS2And H2S can reach State specified standards is discharged, and so as to improve production garden air quality, is improved the working environment of workers, is ensured that worker's body is good for Health.
4th, it is currently preferred, define spray column specification and spray parameter.Can widely it be removed under the parameter a variety of Foul gas, and reach very high removal efficiency.Throughput can be adapted to by adjusting the circular flow of chemical feeding quantity and solution With the change of concentration, therefore there is stronger operating flexibility.The parameter causes the method efficiency high of the present invention, cost is low, effect Good, operation is simpler.
5th, it is currently preferred, define the specification of low-temperature plasma device.Low temperature plasma cracks under the specification Oxidation processes have the advantages that energy consumption is low, processing air quantity is big, it is few to rinse convenient, caused waste water.
Embodiment
Embodiment 1
The administering method of waste gas in a kind of production process of viscose fiber, including following methods step:
A, one-level alkali spray pretreatment
Alkali spray column is connected, forms one-level alkali spray column, carbon disulfide and hydrogen sulfide waste gas by one-level alkali spray column, By interception, collision and the absorption of alkali lye spray and filler, it is volatilizable to remove hydrogen sulfide, a small amount of carbon disulfide and dissolubility Organic compound;
B, reaction is decomposed
Surge tank water removal will be first passed through by the pretreated waste gas of one-level spray column in step A, then pass through pipeline To low-temperature plasma device, the pollutant in waste gas is decomposed, is changed into small molecules fragments;
C, catalysis oxidation
By step B by low-temperature plasma device waste gas be delivered to catalytic oxidation treatment bed reaction, oxidation Decomposition into Pollution-free material;
D, two level alkali spray post processing
Alkali spray column is connected, two level alkali spray column is formed, waste gas of the step C after catalytic oxidation decomposes is led to Cross fiberglass centrifugal blower and introduce described two level alkali spray column, post-processed, gas qualified discharge, absorbing liquid recovery profit With.
During spray, conventional chemical washing equipment is packed absorber, and chemical absorbing liquid is alkaline solution, and chemistry is inhaled Receive liquid down to spray from tower top, waste gas is fully contacted with absorbing liquid, reacted and be removed to upstream, waste gas.
Alkali spray column is together in series as one-level alkali spray column, it is caused useless in spinning process for collecting Gas, in alkali spray column, under being acted on by interception, collision, absorption of the alkali lye and filler of spray etc., hydrogen sulfide and a small amount of two sulphur Change carbon, the volatilizable organic compound of dissolubility can be dissolved down by primary wash, to reduce the subsequently dirt to processing system Dye.This method is easy and effective, and investment is relatively low, is essential pretreating process.
Hydrogen sulfide is substantially achieved removing, and waste gas passes through surge tank(Inside set filler)Water removal, then it is pipelined to low temperature Plasma device, in low-temperature plasma device, the pollutant hair in high energy electron, free radical isoreactivity particle and waste gas Raw effect, contaminant molecule is decomposed within the extremely short time destructions, and follow-up various reactions occur and are degraded with reaching The purpose of pollutant.
Waste gas after low-temperature plasma device is handled passes through catalytic oxidation treatment bed again, makes full use of plasma to produce Ozone in oxidator further molecular fragment fully reacted, supported catalyst is filled out in catalytic oxidation treatment bed fillers It material, can decompose residue ozone and contaminant molecule fragment exhaustive oxidation, and need not frequently change filler, can protect Demonstrate,prove long-term disposal effect.
Finally alkali spray column is together in series as two level alkali spray column.Waste gas after the processing of catalytic oxidation treatment bed is again Two level alkali spray column is introduced by fiberglass centrifugal blower to be handled, two level alkali spray column is absorbable to be oxidized to sulphur simple substance and two The volatility chemical combination organic matter of sulfur oxide, a small amount of sulfur trioxide and small molecule, gas can realize qualified discharge, two level alkali spray column Absorbing liquid can form niter cake, sodium sulphate, when reaching to a certain degree, formed higher concentration metabisulfite solution, can purify or Recycle.
Embodiment 2
On the basis of embodiment 1:
Preferably, the air quantity of the waste gas is 50,000 m3/ h, the one-level alkali spray column is that 2 alkali spray columns are connected, described Two level alkali spray column is that 2 alkali spray columns are connected.
Preferably, the specified tolerance of the low-temperature plasma device is 50,000 m3/ h, peak power 50Kw, input voltage 380v。
Embodiment 3
On the basis of embodiment 1:
Preferably, the air quantity of the waste gas is 100,000 m3/ h, the one-level alkali spray column are that 6 alkali spray columns are connected, institute Two level alkali spray column is stated to connect for 6 alkali spray columns.
Preferably, the specified tolerance of the low-temperature plasma device is 100,000 m3/ h, peak power 80Kw, input voltage 380v。
Embodiment 4
On the basis of embodiment 1:
Preferably, the air quantity of the waste gas is 70,000 m3/ h, the one-level alkali spray column is that 3 alkali spray columns are connected, described Two level alkali spray column is that 3 alkali spray columns are connected.
Preferably, the specified tolerance of the low-temperature plasma device is 70,000 m3/ h, peak power 60Kw, input voltage 380v。
Embodiment 5
On the basis of embodiment 1:
Preferably, the air quantity of the waste gas is 80,000 m3/ h, the one-level alkali spray column is that 5 alkali spray columns are connected, described Two level alkali spray column is that 5 alkali spray columns are connected.
Preferably, the specified tolerance of the low-temperature plasma device is 80,000 m3/ h, peak power 70Kw, input voltage 380v。
Embodiment 6
When the air quantity of the waste gas is 50,000 m3During/h, the one-level alkali spray column is that 2 alkali spray columns are connected, described two Level alkali spray column is that 2 alkali spray columns are connected, and the specification of every spray column is 3600 × 12000mm of Φ.
Preferably, the spray flow 120m of every alkali spray column3/ h, lift 20m, power 11kw, drug concentration 8%.
When the air quantity of the waste gas is 100,000 m3During/h, the one-level alkali spray column is that 6 alkali spray columns are connected, described two Level alkali spray column is that 6 alkali spray columns are connected, and the specification of every spray column is 2600 × 7600mm of Φ.
Preferably, the spray flow 55m of every alkali spray column3/ h, lift 25m, power 11kw, drug concentration 8%.
Embodiment 7
When the air quantity of the waste gas is 50,000 m3During/h, the one-level alkali spray column is that 2 alkali spray columns are connected, described two Level alkali spray column is that 2 alkali spray columns are connected, and the specification of every spray column is 3600 × 12000mm of Φ.
Preferably, the spray flow 120m of every alkali spray column3/ h, lift 20m, power 11kw, drug concentration 10%。
When the air quantity of the waste gas is 100,000 m3During/h, the one-level alkali spray column is that 6 alkali spray columns are connected, described two Level alkali spray column is that 6 alkali spray columns are connected, and the specification of every spray column is 2600 × 7600mm of Φ.
Preferably, the spray flow 55m of every alkali spray column3/ h, lift 25m, power 11kw, drug concentration 10%.
Embodiment 8
When the air quantity of the waste gas is 50,000 m3During/h, the one-level alkali spray column is that 2 alkali spray columns are connected, described two Level alkali spray column is that 2 alkali spray columns are connected, and the specification of every spray column is 3600 × 12000mm of Φ.
Preferably, the spray flow 120m of every alkali spray column3/ h, lift 20m, power 11kw, drug concentration 9%.
When the air quantity of the waste gas is 100,000 m3During/h, the one-level alkali spray column is that 6 alkali spray columns are connected, described two Level alkali spray column is that 6 alkali spray columns are connected, and the specification of every spray column is 2600 × 7600mm of Φ.
Preferably, the spray flow 55m of every alkali spray column3/ h, lift 25m, power 11kw, drug concentration 9%.
Embodiment 9
When the air quantity of the waste gas is 50,000 m3During/h, the one-level alkali spray column is that 2 alkali spray columns are connected, described two Level alkali spray column is that 2 alkali spray columns are connected, and the specification of every spray column is 3600 × 12000mm of Φ.
Preferably, the spray flow 120m of every alkali spray column3/ h, lift 20m, power 11kw, drug concentration 8.5%。
When the air quantity of the waste gas is 100,000 m3During/h, the one-level alkali spray column is that 6 alkali spray columns are connected, described two Level alkali spray column is that 6 alkali spray columns are connected, and the specification of every spray column is 2600 × 7600mm of Φ.
Preferably, the spray flow 55m of every alkali spray column3/ h, lift 25m, power 11kw, drug concentration 8.5%。

Claims (5)

  1. A kind of 1. administering method of waste gas in production process of viscose fiber, it is characterised in that:Including following methods step:
    A, one-level alkali spray pretreatment
    Alkali spray column is connected, one-level alkali spray column, carbon disulfide and hydrogen sulfide waste gas is formed by one-level alkali spray column, passes through Alkali lye sprays and interception, collision and the absorption of filler, removes hydrogen sulfide, a small amount of carbon disulfide and dissolubility is volatilizable has Machine compound;The air quantity of the waste gas is the m3/h of 5-10 ten thousand, and the one-level alkali spray column is connected for 2-6 platform alkali spray column;
    B, reaction is decomposed
    Surge tank water removal will be first passed through by the pretreated waste gas of one-level spray column in step A, then be pipelined to low Isothermal plasma device, the pollutant in waste gas is decomposed, is changed into small molecules fragments;The low-temperature plasma device Specified tolerance is 5-10 ten thousand m3/h, peak power 50-80Kw, input voltage 380v;
    C, catalysis oxidation
    Step B is delivered to the reaction of catalytic oxidation treatment bed by the waste gas of low-temperature plasma device, oxidation Decomposition is into without dirt Contaminate material;
    D, two level alkali spray post processing
    Alkali spray column is connected, forms two level alkali spray column, the two level alkali spray column is connected for 2-6 platform alkali spray column;Will step Rapid waste gas of the C after catalytic oxidation decomposes introduces described two level alkali spray column by fiberglass centrifugal blower, carries out Post processing, gas qualified discharge, absorbing liquid recycle.
  2. 2. the administering method of waste gas in a kind of production process of viscose fiber according to claim 1, it is characterised in that:Work as institute When the air quantity for stating waste gas is 50,000 m3/h, the one-level alkali spray column is that 2 alkali spray columns are connected, and the two level alkali spray column is 2 Platform alkali spray column is connected, and the specification of every spray column is 3600 × 12000mm of Φ.
  3. 3. the administering method of waste gas in a kind of production process of viscose fiber according to claim 2, it is characterised in that:Every The spray flow 120m of the alkali spray column3/ h, lift 20m, power 11kw, drug concentration 8-10%.
  4. 4. the administering method of waste gas in a kind of production process of viscose fiber according to claim 1, it is characterised in that:Work as institute When the air quantity for stating waste gas is 100,000 m3/h, the one-level alkali spray column is that 6 alkali spray columns are connected, and the two level alkali spray column is 6 alkali spray column series connection, the specification of every spray column is 2600 × 7600mm of Φ.
  5. 5. the administering method of waste gas in a kind of production process of viscose fiber according to claim 4, it is characterised in that:Every The spray flow 55m of the alkali spray column3/ h, lift 25m, power 11kw, drug concentration 8-10%.
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CN108452668A (en) * 2018-03-02 2018-08-28 山东派力迪环保工程有限公司 Coke-oven plant's sewage plant waste gas treatment process
CN112237838A (en) * 2020-09-29 2021-01-19 南京格洛特环境工程股份有限公司 System and method for deeply treating low-concentration CS2 by heterogeneous catalytic oxidation technology
CN112206632A (en) * 2020-09-30 2021-01-12 南京格洛特环境工程股份有限公司 Adsorption recovery and heterogeneous catalytic oxidation treatment of CS-containing materials2System for exhaust gas
CN113041823A (en) * 2021-03-18 2021-06-29 武汉三立鼎兴科技有限公司 Carbon disulfide emission control method

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