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GB1338901A - Production of propylene oxide - Google Patents

Production of propylene oxide

Info

Publication number
GB1338901A
GB1338901A GB5168070A GB1338901DA GB1338901A GB 1338901 A GB1338901 A GB 1338901A GB 5168070 A GB5168070 A GB 5168070A GB 1338901D A GB1338901D A GB 1338901DA GB 1338901 A GB1338901 A GB 1338901A
Authority
GB
United Kingdom
Prior art keywords
propylene
carried out
molecular oxygen
gas
oxygen containing
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
GB5168070A
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 GB1338901A publication Critical patent/GB1338901A/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D301/00—Preparation of oxiranes
    • C07D301/02—Synthesis of the oxirane ring
    • C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
    • C07D301/04—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen
    • C07D301/08—Synthesis 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
    • C07D301/10—Synthesis 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/66—Silver or gold
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/06—Halogens; Compounds thereof
    • B01J27/08—Halides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0236—Drying, e.g. preparing a suspension, adding a soluble salt and drying
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements 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)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Epoxy Compounds (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

1338901 Propylene oxide B P CHEMICALS Ltd 13 Oct 1971 [30 Oct 1970] 51680/70 Heading C2C [Also in Division B1] Propylene oxide is prepared by reacting propylene and a molecular oxygen containing gas at an elevated temperature in the presence of a catalyst composition containing elemental silver together with a halide or halides of one or more metals of Group I of the Mendeleef Periodic Table in such a manner that not more than 15% of the total propylene feed is connected per pass. The percentage conversion per pass is defined as total percent C 3 H 6 conversion/recycle ratio and the recycle ratio is defined as flow rate of recycle gas/flow rate of fresh feed gas. The process may be carried out in the vapour phase by passing a gaseous mixture comprising propylene and a molecular oxygen containing gas at an elevated temperature over the catalyst composition. The gaseous reaction mixture may also contain an inert gaseous diluent e.g. helium or nitrogen. The reaction temperature may be in the range 100 to 400‹ C. and the process may be carried out up to about 20 atmos. gauge. The process may also be carried out in the liquid phase by introducing propylene into a reaction zone containing a water immiscible organic solvent carrying a solid suspension of catalyst and thereafter passing a molecular oxygen containing gas e.g. air through the solvent to oxidize the propylene.
GB5168070A 1970-10-30 1970-10-30 Production of propylene oxide Expired GB1338901A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB5168070 1970-10-30

Publications (1)

Publication Number Publication Date
GB1338901A true GB1338901A (en) 1973-11-28

Family

ID=10460979

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5168070A Expired GB1338901A (en) 1970-10-30 1970-10-30 Production of propylene oxide

Country Status (1)

Country Link
GB (1) GB1338901A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
WO1999032471A1 (en) * 1997-12-18 1999-07-01 Arco Chemical Technology, L.P. Epoxidation process using supported silver catalysts treated with carbon dioxide
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
WO2005061472A1 (en) * 2003-12-08 2005-07-07 Lyondell Chemical Technology, L.P. Propylene oxide process

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
WO1998058921A1 (en) * 1997-06-23 1998-12-30 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
CN1107062C (en) * 1997-06-23 2003-04-30 阿科化学技术公司 Propylene expoxidation using chloride-containing silver catalyst
WO1999032471A1 (en) * 1997-12-18 1999-07-01 Arco Chemical Technology, L.P. Epoxidation process using supported silver catalysts treated with carbon dioxide
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
WO2005061472A1 (en) * 2003-12-08 2005-07-07 Lyondell Chemical Technology, L.P. Propylene oxide process
CN100439348C (en) * 2003-12-08 2008-12-03 利安德化学技术有限公司 Propylene oxide process

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Legal Events

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