GB1327497A - Propylene oxide - Google Patents

Propylene oxide

Info

Publication number
GB1327497A
GB1327497A GB2939571A GB1327497DA GB1327497A GB 1327497 A GB1327497 A GB 1327497A GB 2939571 A GB2939571 A GB 2939571A GB 1327497D A GB1327497D A GB 1327497DA GB 1327497 A GB1327497 A GB 1327497A
Authority
GB
United Kingdom
Prior art keywords
propylene
catalyst composition
molecular oxygen
propylene oxide
passing
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
GB2939571A
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.)
BP Chemicals Ltd
Original Assignee
BP Chemicals 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 BP Chemicals Ltd filed Critical BP Chemicals Ltd
Publication of GB1327497A publication Critical patent/GB1327497A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D301/00Preparation of oxiranes
    • C07D301/02Synthesis of the oxirane ring
    • C07D301/03Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
    • C07D301/04Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen
    • C07D301/08Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen in the gaseous phase
    • C07D301/10Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen in the gaseous phase with catalysts containing silver or gold
    • 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
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Epoxy Compounds (AREA)

Abstract

1327497 Propylene oxide BP CHEMICALS INTERNATIONAL Ltd 25 May 1972 [23 June 1971] 29395/71 Heading C2C Propylene oxide is produced in a process which comprises reacting propylene and a molecular oxygen containing gas at an elevated temperature in the presence of a catalyst composition comprising elemental silver together with a halide or halides (as hereinafter defined) of one or more metals of Group II of the Periodic Classification due to Mendeleef. The process may be carried out in the vapour phase by passing a gaseous mixture comprising propylene and a molecular oxygen containing gas over the catalyst composition. The gaseous reaction mixture may also contain an inert gaseous diluent, e.g. helium or nitrogen within the range of 0 to 97% by volume of the mixture. The reaction temperature may be in the range 100‹ to 400‹ C. and the pressure range from atmospheric to 20 atmospheres gauge and the contact time may be 0À1 to 60 seconds. The process may also be carried out in the liquid phase by introducing propylene into a reaction zone containing a water-immiscible organic solvent, e.g. benzene or dimethyl phthalate carrying a solid suspension of catalyst composition and thereafter passing a molecular oxygen containing gas, e.g. air, through the solvent to oxidize the propylene. The term "halide" is defined as any inorganic radical containing a halogen atom e.g. chloride, bromide, fluoride, hypochlorite, hypobromite, chlorate and/or bromate. The produced propylene oxide may be recovered from the reaction mixture by, for example, passing the reaction gases into a gas/liquid scrubbing agent, e.g. cooled ethanol, water and esters of ethylene glycol or propylene glycol, to absorb the oxide, followed by distillation.
GB2939571A 1972-05-25 1972-05-25 Propylene oxide Expired GB1327497A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2939571 1972-05-25

Publications (1)

Publication Number Publication Date
GB1327497A true GB1327497A (en) 1973-08-22

Family

ID=10290901

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2939571A Expired GB1327497A (en) 1972-05-25 1972-05-25 Propylene oxide

Country Status (1)

Country Link
GB (1) GB1327497A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1989007101A1 (en) * 1988-01-28 1989-08-10 Eastman Kodak Company Selective epoxidation of olefins
US4897498A (en) * 1988-01-28 1990-01-30 Eastman Kodak Company Selective monoepoxidation of olefins
WO1998000414A1 (en) * 1996-07-01 1998-01-08 The Dow Chemical Company Process for the direct oxidation of olefins to olefin oxides
US5780657A (en) * 1997-06-23 1998-07-14 Arco Chemical Technology, L.P. Propylene epoxidation using chloride-containing silver catalysts
US6255499B1 (en) 1999-04-08 2001-07-03 The Dow Chemical Company Process for the hydro-oxidation of olefins to olefin oxides using oxidized gold catalyst

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1989007101A1 (en) * 1988-01-28 1989-08-10 Eastman Kodak Company Selective epoxidation of olefins
US4897498A (en) * 1988-01-28 1990-01-30 Eastman Kodak Company Selective monoepoxidation of olefins
US4950773A (en) * 1988-01-28 1990-08-21 Eastman Kodak Company Selective epoxidation of olefins
WO1998000414A1 (en) * 1996-07-01 1998-01-08 The Dow Chemical Company Process for the direct oxidation of olefins to olefin oxides
US5780657A (en) * 1997-06-23 1998-07-14 Arco Chemical Technology, L.P. Propylene epoxidation using chloride-containing silver catalysts
US5965480A (en) * 1997-06-23 1999-10-12 Arco Chemical Technology, L.P. Chloride containing silver catalysts for propylene epoxidation
US6255499B1 (en) 1999-04-08 2001-07-03 The Dow Chemical Company Process for the hydro-oxidation of olefins to olefin oxides using oxidized gold catalyst

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee