JPS5740442A - Production of glycolic ester and ether - Google Patents
Production of glycolic ester and etherInfo
- Publication number
- JPS5740442A JPS5740442A JP55114936A JP11493680A JPS5740442A JP S5740442 A JPS5740442 A JP S5740442A JP 55114936 A JP55114936 A JP 55114936A JP 11493680 A JP11493680 A JP 11493680A JP S5740442 A JPS5740442 A JP S5740442A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- formaldehyde
- glycolic
- ester
- ether
- 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
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
PURPOSE: The reaction between formaldehyde, a caboxylic ester and carbon monoxide in the presence of a strong acid catalyst produces the titled compound used as industrial intermediate of glycolic acid or cellosolves in high yield.
CONSTITUTION: The reaction between formaldehyde such as gaseous formaldehyde or trioxane, a carboxylic ester such as of 1W6C aliphatic acid or monochloroacetic acid, and carbon monoxide is conducted in the presence of a catalyst of strong acid such as hydrochloric acid, hydrobromic acid or trifluoroacetic acid at 25W250°C, preferably 50W200°C to produce the objective compound. The amount of the strong acid is 0.1W1,000meq/mol of formaldehyde. The resultant glycolic ester is hydrolyzed to give glycolic acid, hydrogenated to give ethylene and the hydrogenation of an ether of glycolic acid gives a cellosolve.
COPYRIGHT: (C)1982,JPO&Japio
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55114936A JPS5740442A (en) | 1980-08-21 | 1980-08-21 | Production of glycolic ester and ether |
DE19813107518 DE3107518A1 (en) | 1980-02-29 | 1981-02-27 | Process for the preparation of esters and ethers of glycolic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55114936A JPS5740442A (en) | 1980-08-21 | 1980-08-21 | Production of glycolic ester and ether |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5740442A true JPS5740442A (en) | 1982-03-06 |
JPS6366310B2 JPS6366310B2 (en) | 1988-12-20 |
Family
ID=14650319
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55114936A Granted JPS5740442A (en) | 1980-02-29 | 1980-08-21 | Production of glycolic ester and ether |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5740442A (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59139341A (en) * | 1983-01-20 | 1984-08-10 | Mitsubishi Gas Chem Co Inc | Production of hydroxycarboxylic acid derivative |
JPS59161328A (en) * | 1983-03-01 | 1984-09-12 | Mitsubishi Gas Chem Co Inc | Preparation of hydroxycarbonic acid derivative |
JPS62231106A (en) * | 1986-03-31 | 1987-10-09 | Shimadzu Corp | Optical displacement gauge |
US8466328B2 (en) | 2010-08-18 | 2013-06-18 | Eastman Chemical Company | Method for recovery and recycle of ruthenium homogeneous catalysts |
US8703999B2 (en) | 2012-03-27 | 2014-04-22 | Eastman Chemical Company | Hydrocarboxylation of methylene dipropionate in the presence of propionic acid and a heterogeneous catalyst |
US8709376B2 (en) | 2010-09-23 | 2014-04-29 | Eastman Chemical Company | Process for recovering and recycling an acid catalyst |
US8765999B2 (en) | 2012-03-27 | 2014-07-01 | Eastman Chemical Company | Hydrocarboxylation of formaldehyde in the presence of a higher order carboxylic acid and a homogeneous catalyst |
US8785686B2 (en) | 2010-09-23 | 2014-07-22 | Eastman Chemical Company | Process for recovering and recycling an acid catalyst |
US8829234B2 (en) | 2012-03-27 | 2014-09-09 | Eastman Chemical Company | Hydrocarboxylation of formaldehyde in the presence of a higher order carboxylic acid and heterogeneous catalyst |
US8829248B2 (en) | 2010-08-18 | 2014-09-09 | Eastman Chemical Company | Method for recovery and recycle of ruthenium homogeneous catalysts |
US8927766B2 (en) | 2012-03-27 | 2015-01-06 | Eastman Chemical Company | Hydrocarboxylation of methylene dipropionate in the presence of a propionic acid and a homogeneous catalyst |
US9040748B2 (en) | 2012-06-08 | 2015-05-26 | Eastman Chemical Company | Hydrocarboxylation of aqueous formaldehyde using a dehydrating recycle stream to decrease water concentration |
US9227896B2 (en) | 2010-08-18 | 2016-01-05 | Eastman Chemical Company | Process for the separation and purification of a mixed diol stream |
-
1980
- 1980-08-21 JP JP55114936A patent/JPS5740442A/en active Granted
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59139341A (en) * | 1983-01-20 | 1984-08-10 | Mitsubishi Gas Chem Co Inc | Production of hydroxycarboxylic acid derivative |
JPS59161328A (en) * | 1983-03-01 | 1984-09-12 | Mitsubishi Gas Chem Co Inc | Preparation of hydroxycarbonic acid derivative |
JPS62231106A (en) * | 1986-03-31 | 1987-10-09 | Shimadzu Corp | Optical displacement gauge |
US8829248B2 (en) | 2010-08-18 | 2014-09-09 | Eastman Chemical Company | Method for recovery and recycle of ruthenium homogeneous catalysts |
US8466328B2 (en) | 2010-08-18 | 2013-06-18 | Eastman Chemical Company | Method for recovery and recycle of ruthenium homogeneous catalysts |
US10329230B2 (en) | 2010-08-18 | 2019-06-25 | Eastman Chemical Company | Process for the separation and purification of a mixed diol stream |
US8779214B2 (en) | 2010-08-18 | 2014-07-15 | Eastman Chemical Company | Methods for recovery and recycle of ruthenium homogenous catalysts |
US9227896B2 (en) | 2010-08-18 | 2016-01-05 | Eastman Chemical Company | Process for the separation and purification of a mixed diol stream |
US8709376B2 (en) | 2010-09-23 | 2014-04-29 | Eastman Chemical Company | Process for recovering and recycling an acid catalyst |
US8785686B2 (en) | 2010-09-23 | 2014-07-22 | Eastman Chemical Company | Process for recovering and recycling an acid catalyst |
US8765999B2 (en) | 2012-03-27 | 2014-07-01 | Eastman Chemical Company | Hydrocarboxylation of formaldehyde in the presence of a higher order carboxylic acid and a homogeneous catalyst |
US8927766B2 (en) | 2012-03-27 | 2015-01-06 | Eastman Chemical Company | Hydrocarboxylation of methylene dipropionate in the presence of a propionic acid and a homogeneous catalyst |
US8829234B2 (en) | 2012-03-27 | 2014-09-09 | Eastman Chemical Company | Hydrocarboxylation of formaldehyde in the presence of a higher order carboxylic acid and heterogeneous catalyst |
US8703999B2 (en) | 2012-03-27 | 2014-04-22 | Eastman Chemical Company | Hydrocarboxylation of methylene dipropionate in the presence of propionic acid and a heterogeneous catalyst |
US9040748B2 (en) | 2012-06-08 | 2015-05-26 | Eastman Chemical Company | Hydrocarboxylation of aqueous formaldehyde using a dehydrating recycle stream to decrease water concentration |
Also Published As
Publication number | Publication date |
---|---|
JPS6366310B2 (en) | 1988-12-20 |
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