AU6025180A - Process - Google Patents
ProcessInfo
- Publication number
- AU6025180A AU6025180A AU60251/80A AU6025180A AU6025180A AU 6025180 A AU6025180 A AU 6025180A AU 60251/80 A AU60251/80 A AU 60251/80A AU 6025180 A AU6025180 A AU 6025180A AU 6025180 A AU6025180 A AU 6025180A
- Authority
- AU
- Australia
- Prior art keywords
- branched
- straight
- concentration
- carbon atoms
- hydrogen peroxide
- 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.)
- Abandoned
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/03—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2
Abstract
1. A process for the hydroxylation of 3-chloro-2-methylpropene-1, of straight- or branched- chain monoolefins which are unsubstituted or are already substituted by 1 or 2 hydroxyl groups and have 4 to 7 carbon atoms and a terminal or internal double bond, of straight- or branched- chain monoolefins which are unsubstituted or are already substituted by 1 or 2 hydroxyl groups and have from 8 to 10 carbon atoms and an internal double bond, or of straight- or branched- chain diolefins having from 4 to 10 carbon atoms, characterised in that the olefin to be hydroxylated is reacted at a temperature of from 30 to 80 degrees C with less than 2 mols of formic acid and less than 2 mols of hydrogen peroxide, in each case per mol of double bond to be hydroxylated, formic acid of a concentration of from 20 to 100% by weight is used and hydrogen peroxide of a concentration of less than 50% by weight is used, and the concentration of the hydrogen peroxide in the aqueous phase of the reaction mixture is maintained below 15% by weight for the complete duration of the reaction.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE29378403 | 1979-09-19 | ||
DE2937840A DE2937840C2 (en) | 1979-09-19 | 1979-09-19 | Process for the production of diols, triols or tetrols by hydroxylation of aliphatic mono- or diolefins |
Publications (1)
Publication Number | Publication Date |
---|---|
AU6025180A true AU6025180A (en) | 1981-03-26 |
Family
ID=6081259
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU60251/80A Abandoned AU6025180A (en) | 1979-09-19 | 1980-07-09 | Process |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP0025890B1 (en) |
JP (1) | JPS5936966B2 (en) |
AT (1) | ATE3027T1 (en) |
AU (1) | AU6025180A (en) |
BR (1) | BR8005948A (en) |
CA (1) | CA1218385A (en) |
DE (1) | DE2937840C2 (en) |
ES (1) | ES8104167A1 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2145076A (en) * | 1983-08-13 | 1985-03-20 | Ciba Geigy Ag | A process for producing 1,2-alkanediols |
JPS6045540A (en) * | 1983-08-22 | 1985-03-12 | T Hasegawa Co Ltd | Ethylene glycol derivative |
US4479021A (en) * | 1983-08-30 | 1984-10-23 | Ciba-Geigy Corporation | Continuous process for producing 1,2-alkanediols |
DE3442937C2 (en) * | 1984-11-24 | 1986-11-06 | Degussa Ag, 6000 Frankfurt | Process for the continuous production of 1,2-pentanediol |
DE19743015A1 (en) * | 1997-09-29 | 1999-04-01 | Basf Ag | Process for the preparation of vicinal diols or polyols |
DE102004060541A1 (en) * | 2004-12-15 | 2006-06-29 | Degussa Ag | Process for the preparation of alkanediols and alkanetriols having a vicinal diol group |
DE102013203420A1 (en) | 2013-02-28 | 2014-08-28 | Evonik Industries Ag | Hydrogenolysis of furfuryl alcohol to 1,2-pentanediol |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB634118A (en) * | 1942-02-09 | 1950-03-15 | Bataafsche Petroleum | A process for the catalytic hydroxylation of olefinic compounds |
US2492201A (en) * | 1946-06-07 | 1949-12-27 | Swern Daniel | Hydroxylation process |
FR1047126A (en) * | 1951-12-27 | 1953-12-11 | Gustave Maubec Ets | Preparation of low acid number fatty polyols |
DE956505C (en) * | 1953-01-18 | 1957-01-17 | Ruhrchemie Ag | Process for the production of tricyclo- (5, 2, 1, 0) -dekantriol- (3, 4, 8) or - (3, 4, 9) |
GB1119612A (en) * | 1966-04-20 | 1968-07-10 | W J Bush & Company Ltd | Hydroxylation of alkenyl substituted aromatic compounds |
-
1979
- 1979-09-19 DE DE2937840A patent/DE2937840C2/en not_active Expired
-
1980
- 1980-07-09 AU AU60251/80A patent/AU6025180A/en not_active Abandoned
- 1980-07-09 ES ES493223A patent/ES8104167A1/en not_active Expired
- 1980-08-28 AT AT80105116T patent/ATE3027T1/en not_active IP Right Cessation
- 1980-08-28 EP EP80105116A patent/EP0025890B1/en not_active Expired
- 1980-09-17 BR BR8005948A patent/BR8005948A/en unknown
- 1980-09-17 JP JP55128070A patent/JPS5936966B2/en not_active Expired
- 1980-09-19 CA CA000360664A patent/CA1218385A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE2937840A1 (en) | 1981-04-02 |
BR8005948A (en) | 1981-03-31 |
CA1218385A (en) | 1987-02-24 |
ES493223A0 (en) | 1981-04-16 |
JPS5936966B2 (en) | 1984-09-06 |
EP0025890B1 (en) | 1983-04-13 |
ES8104167A1 (en) | 1981-04-16 |
EP0025890A1 (en) | 1981-04-01 |
ATE3027T1 (en) | 1983-04-15 |
JPS5653627A (en) | 1981-05-13 |
DE2937840C2 (en) | 1985-03-28 |
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