WO2002004116A1 - Procede de preparation d'un catalyseur d'epoxydation - Google Patents

Procede de preparation d'un catalyseur d'epoxydation Download PDF

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Publication number
WO2002004116A1
WO2002004116A1 PCT/EP2001/008008 EP0108008W WO0204116A1 WO 2002004116 A1 WO2002004116 A1 WO 2002004116A1 EP 0108008 W EP0108008 W EP 0108008W WO 0204116 A1 WO0204116 A1 WO 0204116A1
Authority
WO
WIPO (PCT)
Prior art keywords
catalyst
catalyst system
salt
solvent
organic solvent
Prior art date
Application number
PCT/EP2001/008008
Other languages
German (de)
English (en)
Inventor
Andreas Walch
Norbert Rieber
Original Assignee
Basf Aktiengesellschaft
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 Aktiengesellschaft filed Critical Basf Aktiengesellschaft
Priority to AU2001285830A priority Critical patent/AU2001285830A1/en
Publication of WO2002004116A1 publication Critical patent/WO2002004116A1/fr

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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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/48Silver or gold
    • B01J23/50Silver
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/20Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
    • B01J35/23Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Epoxy Compounds (AREA)
  • Catalysts (AREA)

Abstract

La présente invention concerne un procédé de préparation d'un système de catalyse stabilisé. Selon ledit procédé, dans un solvant organique sensiblement anhydre, stable à l'oxydation, est réduit un sel d'un métal du premier, deuxième ou huitième sous-groupe, soluble dans ledit solvant, en présence d'un stabilisant au moyen d'un agent de réduction, pour donner un métal colloïdal. De manière alternative, le sel de métal peut être hydrolysé en présence d'un stabilisant avec de l'eau pour donner un oxyde métallique colloïdal. Le solvant est choisi parmi les hydrocarbures aliphatiques, aromatiques, aliphatiques nitrés et aromatiques nitrés, aliphatiques halogénés et aromatiques halogénés, et en tant que stabilisant est utilisé un stabilisant hydrophobe soluble dans ledit solvant. La sélection du solvant permet d'éviter dans une large mesure les réactions secondaires non désirées telles que la formation de sous-produits tels que les glycols et les glycol monoalkyl éthers. Le système de catalyse ainsi obtenu, ou le catalyseur pouvant être isolé à partir de ce système, peuvent être utilisés pour l'époxydation d'alcènes en solution. Dans un mode de réalisation particulièrement préféré de l'invention, un système de catalyse contenant de l'argent colloïdal est utilisé pour l'époxydation d'éthylène.
PCT/EP2001/008008 2000-07-11 2001-07-11 Procede de preparation d'un catalyseur d'epoxydation WO2002004116A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2001285830A AU2001285830A1 (en) 2000-07-11 2001-07-11 Method for producing an epoxidation catalyst

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10033572A DE10033572A1 (de) 2000-07-11 2000-07-11 Verfahren zur Herstellung eines Epoxidierungskatalysators
DE10033572.1 2000-07-11

Publications (1)

Publication Number Publication Date
WO2002004116A1 true WO2002004116A1 (fr) 2002-01-17

Family

ID=7648481

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2001/008008 WO2002004116A1 (fr) 2000-07-11 2001-07-11 Procede de preparation d'un catalyseur d'epoxydation

Country Status (3)

Country Link
AU (1) AU2001285830A1 (fr)
DE (1) DE10033572A1 (fr)
WO (1) WO2002004116A1 (fr)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5147841A (en) * 1990-11-23 1992-09-15 The United States Of America As Represented By The United States Department Of Energy Method for the preparation of metal colloids in inverse micelles and product preferred by the method
EP0916403A2 (fr) * 1997-11-05 1999-05-19 Director-General Of The Agency Of Industrial Science And Technology Catalyseur pour l'oxydation partielle d'un hydrocarbure et procédé de préparation d'un composé organique contenant de l'oxygène
CN1217328A (zh) * 1997-11-13 1999-05-26 中国石油化工总公司 加压三相系环氧乙烷合成工艺
JPH11253802A (ja) * 1998-03-13 1999-09-21 Nippon Shokubai Co Ltd 液相用エチレン酸化触媒および液相でのエチレンオキシドの製造方法
EP1005907A1 (fr) * 1998-02-24 2000-06-07 Japan as represented by Director-General, Agency of Industrial Science and Technology Catalyseur d'oxydation partielle d'hydrocarbure insature

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5147841A (en) * 1990-11-23 1992-09-15 The United States Of America As Represented By The United States Department Of Energy Method for the preparation of metal colloids in inverse micelles and product preferred by the method
EP0916403A2 (fr) * 1997-11-05 1999-05-19 Director-General Of The Agency Of Industrial Science And Technology Catalyseur pour l'oxydation partielle d'un hydrocarbure et procédé de préparation d'un composé organique contenant de l'oxygène
CN1217328A (zh) * 1997-11-13 1999-05-26 中国石油化工总公司 加压三相系环氧乙烷合成工艺
EP1005907A1 (fr) * 1998-02-24 2000-06-07 Japan as represented by Director-General, Agency of Industrial Science and Technology Catalyseur d'oxydation partielle d'hydrocarbure insature
JPH11253802A (ja) * 1998-03-13 1999-09-21 Nippon Shokubai Co Ltd 液相用エチレン酸化触媒および液相でのエチレンオキシドの製造方法

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Derwent World Patents Index; AN 1999-459238, XP002182599, "Pressure triphase series ethylene oxide process adopt fine particle catalyst three phase bed reactor" *
PATENT ABSTRACTS OF JAPAN vol. 1999, no. 14 22 December 1999 (1999-12-22) *

Also Published As

Publication number Publication date
DE10033572A1 (de) 2002-01-24
AU2001285830A1 (en) 2002-01-21

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