JPS5273810A - Production of glycol monoethers - Google Patents
Production of glycol monoethersInfo
- Publication number
- JPS5273810A JPS5273810A JP50150866A JP15086675A JPS5273810A JP S5273810 A JPS5273810 A JP S5273810A JP 50150866 A JP50150866 A JP 50150866A JP 15086675 A JP15086675 A JP 15086675A JP S5273810 A JPS5273810 A JP S5273810A
- Authority
- JP
- Japan
- Prior art keywords
- production
- glycol monoethers
- pentavalent
- acetal
- reacted
- 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.)
- Granted
Links
Classifications
-
- 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
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
PURPOSE: Acetal is reacted with H2 and CO in the presence of a catalyst composition containing a Co compound and a pentavalent organophosphine oxide to form glycol monoether at a high reaction rate.
COPYRIGHT: (C)1977,JPO&Japio
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50150866A JPS6044290B2 (en) | 1975-12-18 | 1975-12-18 | Method for producing glycol monoether |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50150866A JPS6044290B2 (en) | 1975-12-18 | 1975-12-18 | Method for producing glycol monoether |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5273810A true JPS5273810A (en) | 1977-06-21 |
JPS6044290B2 JPS6044290B2 (en) | 1985-10-02 |
Family
ID=15506078
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP50150866A Expired JPS6044290B2 (en) | 1975-12-18 | 1975-12-18 | Method for producing glycol monoether |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6044290B2 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5754135A (en) * | 1980-09-12 | 1982-03-31 | Texaco Development Corp | |
JPS58134044A (en) * | 1982-02-03 | 1983-08-10 | Mitsubishi Gas Chem Co Inc | Preparation of 2-methoxy-1-propanol |
US8969598B2 (en) | 2011-06-24 | 2015-03-03 | Eastman Chemical Company | Production of cyclic acetals or ketals using liquid-phase acid catalysts |
US9000229B2 (en) | 2011-06-24 | 2015-04-07 | Eastman Chemical Company | Production of hydroxy ether hydrocarbons by vapor phase hydrogenolysis of cyclic acetals and ketals |
US9056313B2 (en) | 2011-06-24 | 2015-06-16 | Eastman Chemical Company | Catalysts for the production of hydroxy ether hydrocarbons by vapor phase hydrogenolysis of cyclic acetals and ketals |
US9315485B2 (en) | 2011-06-24 | 2016-04-19 | Eastman Chemical Company | Production of cyclic acetals by reactive distillation |
US9382179B2 (en) | 2011-06-24 | 2016-07-05 | Eastman Chemical Company | Nickel modified catalyst for the production of hydroxy ether hydrocarbons by vapor phase hydrogenolysis of cyclic acetals and ketals |
US9388105B2 (en) | 2011-06-24 | 2016-07-12 | Eastman Chemical Company | Production of hydroxy ether hydrocarbons by liquid phase hydrogenolysis of cyclic acetals or cyclic ketals |
US9440944B2 (en) | 2011-06-24 | 2016-09-13 | Eastman Chemical Company | Production of cyclic acetals or ketals using solid acid catalysts |
-
1975
- 1975-12-18 JP JP50150866A patent/JPS6044290B2/en not_active Expired
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5754135A (en) * | 1980-09-12 | 1982-03-31 | Texaco Development Corp | |
JPS6039341B2 (en) * | 1980-09-12 | 1985-09-05 | テキサコ・デイベロツプメント・コ−ポレ−シヨン | Method for producing glycol monoalkyl ether and dialkyl ether |
JPS58134044A (en) * | 1982-02-03 | 1983-08-10 | Mitsubishi Gas Chem Co Inc | Preparation of 2-methoxy-1-propanol |
JPH0224260B2 (en) * | 1982-02-03 | 1990-05-29 | Mitsubishi Gas Chemical Co | |
US8969598B2 (en) | 2011-06-24 | 2015-03-03 | Eastman Chemical Company | Production of cyclic acetals or ketals using liquid-phase acid catalysts |
US9000229B2 (en) | 2011-06-24 | 2015-04-07 | Eastman Chemical Company | Production of hydroxy ether hydrocarbons by vapor phase hydrogenolysis of cyclic acetals and ketals |
US9056313B2 (en) | 2011-06-24 | 2015-06-16 | Eastman Chemical Company | Catalysts for the production of hydroxy ether hydrocarbons by vapor phase hydrogenolysis of cyclic acetals and ketals |
US9315485B2 (en) | 2011-06-24 | 2016-04-19 | Eastman Chemical Company | Production of cyclic acetals by reactive distillation |
US9382179B2 (en) | 2011-06-24 | 2016-07-05 | Eastman Chemical Company | Nickel modified catalyst for the production of hydroxy ether hydrocarbons by vapor phase hydrogenolysis of cyclic acetals and ketals |
US9388105B2 (en) | 2011-06-24 | 2016-07-12 | Eastman Chemical Company | Production of hydroxy ether hydrocarbons by liquid phase hydrogenolysis of cyclic acetals or cyclic ketals |
US9394271B2 (en) | 2011-06-24 | 2016-07-19 | Eastman Chemical Company | Production of cyclic acetals or ketals using liquid-phase acid catalysts |
US9440944B2 (en) | 2011-06-24 | 2016-09-13 | Eastman Chemical Company | Production of cyclic acetals or ketals using solid acid catalysts |
Also Published As
Publication number | Publication date |
---|---|
JPS6044290B2 (en) | 1985-10-02 |
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