GB1481895A

GB1481895A – Process for the preparation of glycol ethers
– Google Patents

GB1481895A – Process for the preparation of glycol ethers
– Google Patents
Process for the preparation of glycol ethers

Info

Publication number
GB1481895A

GB1481895A
GB532575A
GB532575A
GB1481895A
GB 1481895 A
GB1481895 A
GB 1481895A
GB 532575 A
GB532575 A
GB 532575A
GB 532575 A
GB532575 A
GB 532575A
GB 1481895 A
GB1481895 A
GB 1481895A
Authority
GB
United Kingdom
Prior art keywords
catalyst
circulated
reaction mixture
glycol ethers
feb
Prior art date
1974-02-09
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
GB532575A
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.)

Hoechst AG

Original Assignee
Hoechst 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.)
1974-02-09
Filing date
1975-02-07
Publication date
1977-08-03

1975-02-07
Application filed by Hoechst AG
filed
Critical
Hoechst AG

1977-08-03
Publication of GB1481895A
publication
Critical
patent/GB1481895A/en

Status
Expired
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

Classifications

C—CHEMISTRY; METALLURGY

C07—ORGANIC CHEMISTRY

C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS

C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups

C07C41/01—Preparation of ethers

C07C41/02—Preparation of ethers from oxiranes

C07C41/03—Preparation of ethers from oxiranes by reaction of oxirane rings with hydroxy groups

Abstract

1481895 Preparation of glycol ethers HOECHST AG 7 Feb 1975 [9 Feb 1974] 5325/75 Heading C2C Glycol ethers are produced by reacting ethylene oxide with a C 1 -C 4 straight or branched chain alcohol in the liquid phase at superatmospheric pressure and a temperature of up to 120‹ C. in a first step in the presence of a solid catalyst, either the catalyst and reaction mixture being circulated or the catalyst being fixed and the reaction mixture circulated, the reaction being completed in a second step either in the presence of the same solid acid catalyst at up to 120‹ C. or in the presence of an alkali at up to 200‹ C. The solid catalyst is for example aluminium hydrosilicate (preferably montmorillonite), silica gel or an acidic ion exchanger. The major product is the monoether of ethylene glycol, with minor amounts of polyglycol ethers, the alcohol: ethylene oxide ratio in the feed being in the range 5.5 : 1 to 11 : 1, the temperature in the main reactor 100‹ C. and the pressure 20 atm. Various reactor layouts are described where the catalyst is either completely circulated with the reaction mixture, circulated in part with the mixture, or is in a fixed bed.

GB532575A
1974-02-09
1975-02-07
Process for the preparation of glycol ethers

Expired

GB1481895A
(en)

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

DE19742406293

DE2406293B1
(en)

1974-02-09
1974-02-09

Process for the production of glycol ethers

Publications (1)

Publication Number
Publication Date

GB1481895A
true

GB1481895A
(en)

1977-08-03

Family
ID=5907044
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

GB532575A
Expired

GB1481895A
(en)

1974-02-09
1975-02-07
Process for the preparation of glycol ethers

Country Status (8)

Country
Link

JP
(1)

JPS50108206A
(en)

BE
(1)

BE825358A
(en)

DE
(1)

DE2406293B1
(en)

ES
(1)

ES434409A1
(en)

FR
(1)

FR2260554B1
(en)

GB
(1)

GB1481895A
(en)

IT
(1)

IT1031560B
(en)

NL
(1)

NL7501303A
(en)

Cited By (3)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US4278820A
(en)

*

1978-10-05
1981-07-14
Showa Denka K.K.
Process for preparing monoalkylene glycol monoethers

US5008465A
(en)

*

1979-12-22
1991-04-16
The British Petroleum Company P.L.C.
Proton-catalyzed reactions catalyzed by hydrogen ion-exchanged layered clays

US5012012A
(en)

*

1987-09-29
1991-04-30
Lion Corporation
Alkoxylation catalyst

Families Citing this family (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US6611106B2
(en)

2001-03-19
2003-08-26
The Regents Of The University Of California
Controlled fusion in a field reversed configuration and direct energy conversion

1974

1974-02-09
DE
DE19742406293
patent/DE2406293B1/en
not_active
Withdrawn

1975

1975-02-03
ES
ES75434409A
patent/ES434409A1/en
not_active
Expired

1975-02-04
NL
NL7501303A
patent/NL7501303A/en
not_active
Application Discontinuation

1975-02-07
IT
IT2006475A
patent/IT1031560B/en
active

1975-02-07
JP
JP1551375A
patent/JPS50108206A/ja
active
Pending

1975-02-07
GB
GB532575A
patent/GB1481895A/en
not_active
Expired

1975-02-10
FR
FR7504044A
patent/FR2260554B1/fr
not_active
Expired

1975-02-10
BE
BE153208A
patent/BE825358A/en
unknown

Cited By (3)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US4278820A
(en)

*

1978-10-05
1981-07-14
Showa Denka K.K.
Process for preparing monoalkylene glycol monoethers

US5008465A
(en)

*

1979-12-22
1991-04-16
The British Petroleum Company P.L.C.
Proton-catalyzed reactions catalyzed by hydrogen ion-exchanged layered clays

US5012012A
(en)

*

1987-09-29
1991-04-30
Lion Corporation
Alkoxylation catalyst

Also Published As

Publication number
Publication date

ES434409A1
(en)

1976-11-16

JPS50108206A
(en)

1975-08-26

FR2260554A1
(en)

1975-09-05

BE825358A
(en)

1975-08-11

DE2406293B1
(en)

1975-05-22

NL7501303A
(en)

1975-08-12

FR2260554B1
(en)

1978-08-18

IT1031560B
(en)

1979-05-10

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(en)

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A process for the production of highly active silver catalysts

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(en)

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Legal Events

Date
Code
Title
Description

1977-12-14
PS
Patent sealed

1982-09-02
PCNP
Patent ceased through non-payment of renewal fee

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