GB1004741A - Process for the purification of gases - Google Patents

Process for the purification of gases

Info

Publication number
GB1004741A
GB1004741A GB1022064A GB1022064A GB1004741A GB 1004741 A GB1004741 A GB 1004741A GB 1022064 A GB1022064 A GB 1022064A GB 1022064 A GB1022064 A GB 1022064A GB 1004741 A GB1004741 A GB 1004741A
Authority
GB
United Kingdom
Prior art keywords
valve
drier
alumina
gas
catalyst
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.)
Expired
Application number
GB1022064A
Inventor
Manfred Davidmann
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.)
BOC Group Ltd
Original Assignee
British Oxigen 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 British Oxigen Ltd filed Critical British Oxigen Ltd
Priority to GB1022064A priority Critical patent/GB1004741A/en
Publication of GB1004741A publication Critical patent/GB1004741A/en
Expired legal-status Critical Current

Links

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
    • B01D53/86Catalytic 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
    • 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
    • B01D53/26Drying gases or vapours
    • B01D53/261Drying gases or vapours by adsorption

Landscapes

  • 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)
  • Drying Of Gases (AREA)

Abstract

Inert gases, e.g. nitrogen, argon, are purified by adding a reactant before or after compression of the gas to react with the impurities to form water, catalytically reacting the mixture and removing water with a desiccant, the heat of compression being used to simultaneously regenerate desiccant. The desiccant may be alumina or silica gel and the catalyst may be e.g. palladium "promoted" on pelleted alumina. The gas, containing say oxygen impurity, with the requisite amount of added hydrogen enters at 13 and is compressed in compressor 14 so that it leaves as a hot gas and enters the catalyst reaction chamber 12. Part or all of the hot gas leaving the compressor by-passes the catalyst chamber 12 through valves 17, 18 and passes upwardly through drier 11 to remove moisture retained by the alumina therein. The moist gas from 11 then passes through valve 19 to catalyst chamber 12 whence it is passed to water cooler 20 to condense part of the water which is collected in vessel 21, and proceeds through 21 and valve 22 to operating drier 10. The dried and purified gas leaves through valve 23. When regeneration of alumina in drier 11 is complete, valve 17 is closed and valve 24 is opened to by-pass the hot gas from compressor 14 through water cooler 26. The cooled gas passes <PICT:1004741/C1/1> through valve 18 and upwardly through drier 11 to cool the alumina therein. After the alumina has cooled, valves 18, 19, 22, 23, 24 are closed and valve 17 opened so that the drier 10 is regenerated and drier 11 operated. Alumina in drier 10 is cooled by closing valve 17 and opening valve 24. In an alternative method, two catalyst vessels in series and two driers are used.
GB1022064A 1964-03-11 1964-03-11 Process for the purification of gases Expired GB1004741A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1022064A GB1004741A (en) 1964-03-11 1964-03-11 Process for the purification of gases

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1022064A GB1004741A (en) 1964-03-11 1964-03-11 Process for the purification of gases

Publications (1)

Publication Number Publication Date
GB1004741A true GB1004741A (en) 1965-09-15

Family

ID=9963823

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1022064A Expired GB1004741A (en) 1964-03-11 1964-03-11 Process for the purification of gases

Country Status (1)

Country Link
GB (1) GB1004741A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2173182A (en) * 1985-03-28 1986-10-08 Boc Group Inc Methods and apparatus for purifying inert gas streams
EP0395221A1 (en) * 1989-03-29 1990-10-31 The Boc Group, Inc. Method of reducing the oxygen concentration in a gas stream
NL9301372A (en) * 1993-08-06 1995-03-01 Delair Droogtech & Lucht Air drying system, and method for operating the system
WO2000073202A1 (en) * 1999-05-26 2000-12-07 Solutia Inc. Process for nitrous oxide purification
WO2001078869A1 (en) * 2000-04-19 2001-10-25 Saes Getters S.P.A. A process for the purification of organometallic compounds or heteroatomic organic compounds with a palladium-based catalyst
CN114929362A (en) * 2020-01-02 2022-08-19 阿特拉斯·科普柯空气动力股份有限公司 Drying device and method for drying compressed gas

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2173182A (en) * 1985-03-28 1986-10-08 Boc Group Inc Methods and apparatus for purifying inert gas streams
GB2173182B (en) * 1985-03-28 1989-06-21 Boc Group Inc Methods and apparatus for purifying inert gas streams
EP0395221A1 (en) * 1989-03-29 1990-10-31 The Boc Group, Inc. Method of reducing the oxygen concentration in a gas stream
NL9301372A (en) * 1993-08-06 1995-03-01 Delair Droogtech & Lucht Air drying system, and method for operating the system
WO2000073202A1 (en) * 1999-05-26 2000-12-07 Solutia Inc. Process for nitrous oxide purification
WO2001078869A1 (en) * 2000-04-19 2001-10-25 Saes Getters S.P.A. A process for the purification of organometallic compounds or heteroatomic organic compounds with a palladium-based catalyst
CN114929362A (en) * 2020-01-02 2022-08-19 阿特拉斯·科普柯空气动力股份有限公司 Drying device and method for drying compressed gas
CN114929362B (en) * 2020-01-02 2024-04-26 阿特拉斯·科普柯空气动力股份有限公司 Drying device and method for drying compressed gas

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