GB835751A - Improvements in the removal of impurities from gases or vapours - Google Patents

Improvements in the removal of impurities from gases or vapours

Info

Publication number
GB835751A
GB835751A GB20964/56A GB2096456A GB835751A GB 835751 A GB835751 A GB 835751A GB 20964/56 A GB20964/56 A GB 20964/56A GB 2096456 A GB2096456 A GB 2096456A GB 835751 A GB835751 A GB 835751A
Authority
GB
United Kingdom
Prior art keywords
hydrogen
compounds
mixture
oxygen
nitrogen
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
GB20964/56A
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.)
BASF SE
Original Assignee
BASF SE
Badische Anilin and Sodafabrik AG
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 BASF SE, Badische Anilin and Sodafabrik AG filed Critical BASF SE
Publication of GB835751A publication Critical patent/GB835751A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • 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
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/151Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Abstract

In a process for the removal of impurities from a gas or vapours, the gas or vapour is passed over a mixture comprising a copper compound which has been precipitated together with or on to a precipitate of one or more compounds of magnesium and/or iron and optionally cobalt and/or nickel. Suitable compounds are the hydroxides, carbonates and silicates and the weight ratio of copper to the other metals in the mixture may vary between 1 : 20 and 20 : 1, preferably lying between 1 : 2 and 2 : 1. Small amounts of compounds of the alkaline earth metals, zinc, cadmium, chromium, molybdenum, tungsten, vanadium, uranium, titanium and/or thorium, singly or in admixture with one another may be incorporated in the mixture. The purification may be carried out at any pressure or reduced pressure and at room temperature or a temperature below 0 DEG C. or at an elevated temperature. The mixture may be reduced, e.g. with hydrogen at between 80 DEG and 150 DEG C., before use as a purifying material. Impurities which can be removed are inorganic and organic sulphur compounds, oxygen, formaldehyde, acetylene and its homologues, halogens and their compounds, e.g. hydrochloric acid and vinyl chloride, hydrogen cyanide; pyridine, nitrogen di-oxide, nitric acid, carbon monoxide, metal carbonyls and ammonia. Gases or vapours which can be purified are nitrogen, carbon dioxide, ethylene, propylene or other gaseous hydrocarbons or their derivatives, hydrogen or synthesis gases or cracking gases containing hydrogen in admixture with carbon monoxide or nitrogen, and the vapours of liquid hydrocarbons such as gasoline or benzene. In described applications of the process oxygen is removed from air to obtain nitrogen, oxygen, acetylene and hydrogen sulphide are removed from ethylene or propylene, hydrogen sulphide is removed from carbon di-oxide, oxygen is removed from hydrogen, organic sulphur compounds are removed from hydrogen and thiophene is removed from benzene in the presence of hydrogen. Regeneration of exhausted purifying material may be effected by oxidation or reduction at an elevated temperature, e.g. by reduction with hydrogen at 150 DEG C., or when the material has been used to remove acetylene by passing nitrogen over the material.ALSO:In a process for the removal of impurities from a gas or vapour, the gas or vapour is passed over a mixture comprising a copper compound which has been precipitated together with or on to a precipitate of one or more compounds of magnesium and/or iron and optionally cobalt and/or nickel. Suitable compounds are the hydroxides, carbonates and silicates and the weight ratio of copper to the other metals in the mixture may vary between 1 : 20 to 20 : 1, preferably lying between 1 : 2 and 2 : 1. Small amounts of compounds of the alkaline earth metals, zinc, cadmium, chromium, molybdenum, tungsten, vanadium, uranium, titanium and thorium, singly or in admixture with one another may be incorporated in the mixture. The purification may be carried out at any pressure or reduced pressure and at room temperature or a temperature below 0 DEG C. or at an elevated temperature. The mixture may be reduced, e.g. with hydrogen at between 80 DEG and 150 DEG C., before use as a purifying material. Impurities which can be removed are inorganic and organic sulphur compounds, oxygen, formaldehyde, acetylene and its homologues, halogens and their compounds, e.g. hydrochloric acid and vinyl chloride, nitric acid, carbon monoxide, metal carbonyls, and ammonia. Gases or vapours which can be purified are nitrogen, carbon dioxide, ethylene, propylene or other gaseous hydrocarbons or their derivatives, hydrogen or synthesis gases or cracking gases containing hydrogen in admixture with carbon monoxide or nitrogen, and the vapours of liquid hydrocarbons such as gasoline or benzene. In described applications of the process oxygen is removed from air to obtain nitrogen, oxygen, acetylene and hydrogen sulphide are removed from ethylene or propylene, hydrogen sulphide is removed from carbon di-oxide, oxygen is removed from hydrogen, organic sulphur compounds are removed from hydrogen and thiophene is removed from benzene in the presence of hydrogen. Regeneration of exhausted purifying material may be effected by oxidation or reduction at an elevated temperature, e.g. by reduction with hydrogen at 150 DEG C., or when the material has been used to remove acetylene by passing nitrogen over the material.
GB20964/56A 1955-07-13 1956-07-06 Improvements in the removal of impurities from gases or vapours Expired GB835751A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE835751X 1955-07-13

Publications (1)

Publication Number Publication Date
GB835751A true GB835751A (en) 1960-05-25

Family

ID=6760995

Family Applications (1)

Application Number Title Priority Date Filing Date
GB20964/56A Expired GB835751A (en) 1955-07-13 1956-07-06 Improvements in the removal of impurities from gases or vapours

Country Status (1)

Country Link
GB (1) GB835751A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3306707A (en) * 1963-07-01 1967-02-28 Universal Oil Prod Co Hydrogen producing system with hydrocarbon stripping of regenerated catalyst
US3390102A (en) * 1966-12-01 1968-06-25 Catalysts & Chemicals Inc Reduction-activation of copper oxidezinc oxide low temperature shift catalysts
DE1929977A1 (en) * 1968-06-17 1969-12-18 Stamicarbon Process for the purification of olefins
GB2155452A (en) * 1983-10-26 1985-09-25 John Thomas Mccullins Active adsorption media for oxygen and water vapour
US5777058A (en) * 1994-01-10 1998-07-07 Atmi Ecosys Corporation Metallo-oxomeric scrubber compositions
WO2012063034A3 (en) * 2010-11-11 2012-09-27 Johnson Matthey Public Limited Company Process
CN112933985A (en) * 2021-01-29 2021-06-11 三明学院 Thiophene selective molybdenum diselenide vertical graphene hybrid film, preparation method thereof and thiophene separation method

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3306707A (en) * 1963-07-01 1967-02-28 Universal Oil Prod Co Hydrogen producing system with hydrocarbon stripping of regenerated catalyst
US3390102A (en) * 1966-12-01 1968-06-25 Catalysts & Chemicals Inc Reduction-activation of copper oxidezinc oxide low temperature shift catalysts
DE1929977A1 (en) * 1968-06-17 1969-12-18 Stamicarbon Process for the purification of olefins
GB2155452A (en) * 1983-10-26 1985-09-25 John Thomas Mccullins Active adsorption media for oxygen and water vapour
US5777058A (en) * 1994-01-10 1998-07-07 Atmi Ecosys Corporation Metallo-oxomeric scrubber compositions
WO2012063034A3 (en) * 2010-11-11 2012-09-27 Johnson Matthey Public Limited Company Process
GB2499742A (en) * 2010-11-11 2013-08-28 Johnson Matthey Plc Process
CN103380199A (en) * 2010-11-11 2013-10-30 庄信万丰股份有限公司 Process
US9057036B2 (en) 2010-11-11 2015-06-16 Johnson Matthey Plc Process for generating a synthetic natural gas
CN112933985A (en) * 2021-01-29 2021-06-11 三明学院 Thiophene selective molybdenum diselenide vertical graphene hybrid film, preparation method thereof and thiophene separation method

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