CN107321171A - A kind of Phosphine gas purifier - Google Patents

A kind of Phosphine gas purifier Download PDF

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Publication number
CN107321171A
CN107321171A CN201710456177.6A CN201710456177A CN107321171A CN 107321171 A CN107321171 A CN 107321171A CN 201710456177 A CN201710456177 A CN 201710456177A CN 107321171 A CN107321171 A CN 107321171A
Authority
CN
China
Prior art keywords
clean unit
filter element
main casing
phosphine
gas
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.)
Withdrawn
Application number
CN201710456177.6A
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Chinese (zh)
Inventor
陈道斌
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Suzhou Bohan Environmental Protection Technology Co Ltd
Original Assignee
Suzhou Bohan Environmental Protection Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Suzhou Bohan Environmental Protection Technology Co Ltd filed Critical Suzhou Bohan Environmental Protection Technology Co Ltd
Priority to CN201710456177.6A priority Critical patent/CN107321171A/en
Publication of CN107321171A publication Critical patent/CN107321171A/en
Withdrawn legal-status Critical Current

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Classifications

    • 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
    • B01D53/81Solid phase processes
    • B01D53/82Solid phase processes with stationary reactants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/10Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
    • 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
    • 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
    • B01D53/8671Removing components of defined structure not provided for in B01D53/8603 - B01D53/8668
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/55Compounds of silicon, phosphorus, germanium or arsenic

Abstract

The invention discloses a kind of Phosphine gas purifier, it is desirable to provide a kind of, environmental protection equipment that safe and reliable, operating cost low high to phosphine gas purification efficiency.Phosphine gas purifier includes air inlet, front end diffuser, filter element, neck, framed bent, clean unit, bracket, filter element cover plate, main casing, clean unit cover plate, pressing handwheel, end diffuser and gas outlet, be it is a kind of at normal temperatures to the industrial waste gas of phosphine containing after primary purification can the cleaning equipment directly up to standard that be discharged into air, processing air quantity is 500~50000m3The concentration of hydrogen phosphide is not more than 0.3mg/m in gas after/h, purification3

Description

A kind of Phosphine gas purifier
Technical field
It is a kind of environment protection equipment the present invention relates to a kind of Phosphine gas purifier, at normal temperatures will be phosphorous Air is directly discharged into after the industrial waste gas purifying of change hydrogen is up to standard.
Background technology
The fumigant insect killing that phosphine gas is widely used in the storage sectors such as tobacco, grain, leather, Chinese herbal medicine and linen-cotton is made Industry.Overwhelming majority enterprise just directly discharges the poisonous phosphine gas in warehouse after insecticidal operation without purified treatment at present, Ambient atmosphere environment is polluted, the safeguard procedures taken generally set certain safe distance around warehouse, make discharge Phosphine gas concentration be substantially diluted.The domestic research to the purifier of phosphine gas is started late, at present to phosphorus Change hydrogen carry out purified treatment equipment mainly have packed tower purifier, bubbling and spraying combination purification device, bubbling and Spray combination purification device, light degradation purifier, combustion purification device and pressure swing adsorption purge device etc..
Chinese patent CN2456825Y, CN2456822Y, CN201320445Y, CN201300033Y and The device for purifying phosphine gas of the announcements such as CN200999201Y is based on liquid phase reactor, and feature is purified with liquid phase scrubbing method The efficiency of processing hydrogen phosphide is restricted by oxidant concentration height in liquid phase, when equipment works, the purification efficiency of phosphine gas Fluctuation is larger, when gas is directly discharged in air after purification, however it remains the problem of being unable to qualified discharge, if will purification Gas not up to standard afterwards is sent storehouse back to and circulated to be purified again, then sacrifices processing air quantity, add the clarification time.
The device for purifying phosphine gas that Chinese patent CN2442687Y is announced is based on solid phase reaction, and feature is stifling Phosphine gas in storehouse is flowed through after filter, is sent back to again in storehouse and is carried out multiple iterative cycles until up to standard, in order to allow Gas is formed in storehouse to be needed to lay a large amount of pipe specials in circulation, storehouse, occupies effective storage, meanwhile, circularly purifying must So rate of ventilation in increase storehouse, extends the clarification time.
It is special based on the hydrogen phosphide purification processing unit that Chinese patent CN101959322A is announced is reacted with ultraviolet degradation Point is the back-shaped pipeline that phosphine fumigation exhaust gas is made up of light transmissive material, degrades, then flows back under ultraviolet light Stifling closed environment.Using circularly purifying mode, increase rate of ventilation in storehouse, extend the clarification time, sent out using ultraviolet source Light, energy consumption is big, operating cost is high.
The hydrogen phosphide purification processing method that Chinese patent CN101732962A is announced, uses the caustic wash tower list of filling ceramic ring Member and 2 column precious metal palladium charcoal catalytic oxidation units, are entered after phosphine containing industrial waste gas is preheated by reaction tower bottom, Tower top is flowed out, and heating and thermal insulation is carried out to reaction tower with vapours, temperature be 100~150 DEG C, handle air quantity and be 36~ 50m3During/h, its purification efficiency reaches that phosphine gas concentration is less than 1.0mg/m after 99.8%, purification3.Handle air quantity small, no The normal temperature purified treatment of hydrogen phosphide can be realized, high energy consumption, operating cost are high.
Several purifiers are carried out after purified treatment to the industrial waste gas of phosphine containing above, and not only primary purification directly reaches Mark discharge is difficult, and processing air quantity is small, is not suitable for applying on large warehoused.
The content of the invention
Primary purification is carried out to phosphine gas after storage fumigant insect killing it is an object of the invention to provide one kind directly up to standard The poisonous Phosphine gas purifier of Wind Volume of discharge.
The Phosphine gas purifier that the present invention is provided includes air inlet, front end diffuser, filter element, framed bent, purification Unit, bracket, filter element cover plate, main casing, clean unit cover plate, pressing handwheel, end diffuser and gas outlet.Front end is expanded Dissipate device and end diffuser is located at clarifier main casing both sides, filter element, neck, framed bent, clean unit and bracket are located at Inside clarifier main casing, filter element is designed using plank frame, is fixed in neck, with the filtering positioned at main casing body side surface Unit cover is sealed;Clean unit uses columnar structured design, and one end is fixed on framed bent, and the other end is fixed on bracket, Clean unit cover plate is located at the side of clarifier main casing, is fixed by pressing handwheel.
Filter element and clean unit can be changed after the once above fumigant insect killing end of job, and clean unit can be according to place The size of air quantity is managed by 5~200 parallel combinations.
Filter element is a kind of device that effective detention purpose is played to dust in air, impurity, or even aerosol.Using Plank frame is designed, and is typically made up of thick effect, medium air filtration medium, high-efficiency filtration media can also be used in some special occasions, Improve detention efficiency.
A diameter of 100~1000mm of clean unit, is highly 200~2400mm, processing air quantity be 50~ 500m3/h ;Scavenging material is seated in clean unit, and scavenging material can be with zeolite, molecular sieve, diatomite, three oxidations two Aluminium or activated carbon is in the impregnated catalysts or potassium permanganate, manganese dioxide, silver nitrate, copper sulphate, copper acetate of carrier One or more of solid particulate matters formed.When the industrial waste gas of phosphine containing passes through clean unit, hydrogen phosphide is thorough Absorbing reaction is fallen, and does not produce secondary pollution, plays the purpose of environmental protection and periphery personnel health.
Filter element cover plate and clean unit cover plate are respectively arranged at the side of clarifier main casing, are easy to load and unload and change Filter element and clean unit, and play a part of seal casinghousing.
During present invention work, the impurity such as dust, particulate matter in warehouse can be made by the effective detention of filter element, protection is played The purpose of scavenging material in clean unit.Meanwhile, poisonous phosphine gas is complete with scavenging material reaction in clean unit, raw Stayed in into phosphoric acid in scavenging material, effectively prevent the pollution to ambient atmosphere environment, it is ensured that the personal safety of periphery personnel.
The present invention handles air quantity from 500m3/ h to 50000m3/ h, purification reaction is carried out at normal temperatures, after primary purification The concentration of hydrogen phosphide is not more than 0.3mg/m in gas3, can be directly discharged into air.
Brief description of the drawings
Accompanying drawing is schematic structural view of the invention.
1. the support of 6. clean unit of air inlet 2. front end diffuser, 3. filter element, 4. neck, 5. framed bent 7. The end diffuser 13. of 11. pressing handwheel of frame 8. filter element cover plate, 9. main casing, 10. clean unit cover plate 12. Gas outlet.
Embodiment
In accompanying drawing Phosphine gas purifier include air inlet 1, front end diffuser 2, filter element 3, neck 4, framed bent 5, Clean unit 6, bracket 7, filter element cover plate 8, main casing 9, clean unit cover plate 10, pressing handwheel 11, end diffuser 12 With gas outlet 13;Front end diffuser 2 and end diffuser 12 are located at the both sides of clarifier main casing 9, filter element 3, neck 4th, framed bent 5, clean unit 6 and bracket 7 are located inside clarifier main casing 9, and filter element 3 is set using plank frame Meter, is fixed in neck 4, is sealed with the filter element cover plate 8 positioned at the side of main casing 9;Clean unit 6 uses cylindrical shape Structure design, one end is fixed on framed bent 5, and the other end is fixed on bracket 7, and clean unit cover plate 10 is located at clarifier The side of main casing 9, is fixed by pressing handwheel 11.
Embodiment 1:
Phosphine gas purifier, processing air quantity is 2000m3/ h, it is net comprising 16 a diameter of 200mm, highly for 500mm Change unit, scavenging material is potassium permanganate solid particulate matter.For the tail gas after the pen bank phosphine fumigation end of job Purification, phosphine gas concentration is 270mg/m in storehouse when purification starts3, phosphine gas is dense in storehouse after purifying 30 hours Degree is less than 1mg/m3, the concentration of hydrogen phosphide is not more than 0.3mg/m in gas after being handled through the clarifier3, air can be directly discharged into In.
Embodiment 2:
Phosphine gas purifier, processing air quantity is 30000m3/ h, comprising 180 a diameter of 300mm, highly be 2000mm Clean unit, scavenging material is impregnated catalyst using activated carbon as carrier.For large-scale tobacco leaf storage storehouse phosphine fumigation Tail gas clean-up after the end of job, phosphine gas concentration is 530mg/m in storehouse when purification starts3, stored in a warehouse after purifying 30 hours Phosphine gas concentration is less than 1mg/m in storehouse3, hydrogen phosphide is not detected by gas after being handled through the clarifier, can be directly discharged into In air.

Claims (3)

1. a kind of Phosphine gas purifier, it is characterized in that clarifier includes air inlet (1), front end diffuser (2), filter element (3), neck (4), framed bent (5), clean unit (6), bracket (7), filter element cover plate (8), main casing (9), clean unit lid Plate (10), pressing handwheel (11), end diffuser (12) and gas outlet (13);Front end diffuser (2) and end diffuser (12) it is located at clarifier main casing (9) both sides, filter element (3), neck (4), framed bent (5), clean unit (6) and bracket (7) it is located at clarifier main casing (9) internal, filter element (3) is fixed in neck (4) using plank frame design, is used Filter element cover plate (8) positioned at main casing (9) side is sealed;Clean unit (6) uses columnar structured design, one end It is fixed on framed bent (5), the other end is fixed on bracket (7), clean unit cover plate (10) is located at clarifier main casing (9) Side, it is fixed by pressing handwheel (11).
2. the Phosphine gas purifier according to claim 1, it is characterized in that a diameter of the 100 of clean unit (6)~ 1000mm, is highly 200~2400mm, and processing air quantity is 50~500m3/h ;Scavenging material is seated in clean unit (6) In, scavenging material is the impregnated catalyst using zeolite, molecular sieve, diatomite, alundum (Al2O3) or activated carbon as carrier.
3. the Phosphine gas purifier according to claim 1, it is characterized in that clarifier contains 5~200 purification lists First (6), matched combined in parallel, processing air quantity is 500~50000m3/h。
CN201710456177.6A 2017-06-16 2017-06-16 A kind of Phosphine gas purifier Withdrawn CN107321171A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710456177.6A CN107321171A (en) 2017-06-16 2017-06-16 A kind of Phosphine gas purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710456177.6A CN107321171A (en) 2017-06-16 2017-06-16 A kind of Phosphine gas purifier

Publications (1)

Publication Number Publication Date
CN107321171A true CN107321171A (en) 2017-11-07

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710456177.6A Withdrawn CN107321171A (en) 2017-06-16 2017-06-16 A kind of Phosphine gas purifier

Country Status (1)

Country Link
CN (1) CN107321171A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112047316A (en) * 2020-08-31 2020-12-08 江苏康祥实业集团有限公司 Heterogeneous catalysis treatment method for sodium hypophosphite tail gas

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202146710U (en) * 2011-01-04 2012-02-22 中国人民解放军63971部队 Phosphine gas purifier

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202146710U (en) * 2011-01-04 2012-02-22 中国人民解放军63971部队 Phosphine gas purifier

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112047316A (en) * 2020-08-31 2020-12-08 江苏康祥实业集团有限公司 Heterogeneous catalysis treatment method for sodium hypophosphite tail gas

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Application publication date: 20171107

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