GB846077A - Improvements in or relating to the purification of ethylene - Google Patents

Improvements in or relating to the purification of ethylene

Info

Publication number
GB846077A
GB846077A GB9231/59A GB923159A GB846077A GB 846077 A GB846077 A GB 846077A GB 9231/59 A GB9231/59 A GB 9231/59A GB 923159 A GB923159 A GB 923159A GB 846077 A GB846077 A GB 846077A
Authority
GB
United Kingdom
Prior art keywords
oxygen
catalyst
present
carbon monoxide
rhodium
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
GB9231/59A
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.)
Engelhard Industries Inc
Original Assignee
Engelhard Industries Inc
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 Engelhard Industries Inc filed Critical Engelhard Industries Inc
Publication of GB846077A publication Critical patent/GB846077A/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
    • C10K3/02Modifying 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 by catalytic treatment
    • C10K3/04Modifying 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 by catalytic treatment reducing the carbon monoxide content, e.g. water-gas shift [WGS]
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/148Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
    • C07C7/14808Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound with non-metals as element
    • C07C7/14816Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound with non-metals as element oxygen; ozone

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • Analytical Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Catalysts (AREA)

Abstract

Carbon monoxide is removed from ethylene by selective oxidation by passing with oxygen over a rhodium-containing catalyst at 25-150 DEG C.; if acetylene and hydrogen are also present the acetylene is selectively hydrogenated. The rhodium catalyst may be mixed with another platinum metal, particularly platinum and supported on activated alumina, silica, silica gel, or kieselguhr. The gas is passed over the catalyst at a rate of 100-5,000 standard volumes per hour per volume of catalyst at 0-1,000 p.s.i.g. The oxygen should be present in at least the stoichiometric amount for reaction with carbon monoxide and may be present in up to 20 times this amount. Many gas mixtures frequently contain sufficient oxygen, otherwise oxygen or air is added.ALSO:Carbon monoxide present in ethylene is selectively oxidised to carbon dioxide by oxygen at 25-150 DEG C. over a catalyst containing rhodium and optionally another platinum metal, preferably platinum. The catalyst may be supported on activated alumina, silica, silica gel, kieselguhr or diatomaceous earth. Flow rates of 100-5,000 vol./vol./hr. are used at pressures of 0-1,000 p.s.i.g. Oxygen may be present in amounts of 1-20 times the stoichiometric quantity for combining with the carbon monoxide.
GB9231/59A 1958-03-19 1959-03-17 Improvements in or relating to the purification of ethylene Expired GB846077A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US846077XA 1958-03-19 1958-03-19

Publications (1)

Publication Number Publication Date
GB846077A true GB846077A (en) 1960-08-24

Family

ID=22186062

Family Applications (1)

Application Number Title Priority Date Filing Date
GB9231/59A Expired GB846077A (en) 1958-03-19 1959-03-17 Improvements in or relating to the purification of ethylene

Country Status (1)

Country Link
GB (1) GB846077A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8193374B2 (en) 2008-05-15 2012-06-05 Shell Oil Company Process for the preparation of alkylene carbonate and/or alkylene glycol
US8273912B2 (en) 2008-05-15 2012-09-25 Shell Oil Company Process for the preparation of an alkylene carbonate and an alkylene glycol
US9144765B2 (en) 2007-05-18 2015-09-29 Shell Oil Company Reactor system, an absorbent and a process for reacting a feed

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9144765B2 (en) 2007-05-18 2015-09-29 Shell Oil Company Reactor system, an absorbent and a process for reacting a feed
US8193374B2 (en) 2008-05-15 2012-06-05 Shell Oil Company Process for the preparation of alkylene carbonate and/or alkylene glycol
US8273912B2 (en) 2008-05-15 2012-09-25 Shell Oil Company Process for the preparation of an alkylene carbonate and an alkylene glycol
US8858893B2 (en) 2008-05-15 2014-10-14 Shell Oil Company Process for the preparation of an alkylene carbonate and an alkylene glycol
US9527787B2 (en) 2008-05-15 2016-12-27 Shell Oil Company Process for the preparation of alkylene carbonate and/or alkylene glycol

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