GB688553A - Manufacture of glycols - Google Patents
Manufacture of glycolsInfo
- Publication number
- GB688553A GB688553A GB1278550A GB1278550A GB688553A GB 688553 A GB688553 A GB 688553A GB 1278550 A GB1278550 A GB 1278550A GB 1278550 A GB1278550 A GB 1278550A GB 688553 A GB688553 A GB 688553A
- Authority
- GB
- United Kingdom
- Prior art keywords
- dimethylpentane
- diol
- methacrolein
- hydrogenated
- naoh
- 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.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C43/00—Ethers; Compounds having groups, groups or groups
- C07C43/02—Ethers
- C07C43/03—Ethers having all ether-oxygen atoms bound to acyclic carbon atoms
- C07C43/04—Saturated ethers
- C07C43/13—Saturated ethers containing hydroxy or O-metal groups
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention comprises a new compound, 2 - n - butoxymethyl - 2 : 4 - dimethylpentane-1 : 5 diol, and a process for the manufacture of diols of the general formula <FORM:0688553/IV (b)/1> in which R1 is methyl or ethyl and R2 is a straight chain alkyl radical of not more than 4 carbon atoms, by treating a substituted acrolein of formula CH2 = C(R1)-CHO with dilute aqueous alkali and an alcohol R2OH at temperatures not exceeding 50 DEG C. and subjecting the product, preferably after isolation from the reaction mixture, to catalytic hydrogenation. Cooling is necessary to maintain the temperature in the desired range for the condensation process as the reaction is exothermic. The hydrogenation is preferably carried out at a temperature in the range 50-200 DEG C. and at a pressure above 50 atm. in the presence of Raney nickel paste. In the examples (a) a -methacrolein is condensed with methanol in the presence of NaOH and the resulting product is separated and hydrogenated to give 2-methoxymethyl-2,4-dimethylpentane-1.5 diol; (b) a -methacrolein is condensed with ethanol in the presence of NaOH and the resulting compound, after separation, is hydrogenated to give 2-ethoxymethyl-2 : 4-dimethylpentane-1 : 5-diol; (c) a -methacrolein is condensed with n-butanol in the presence of NaOH and the product, after separation, is hydrogenated to give a new compound 2-n-butoxymethyl-2 : 4-dimethylpentane-1 : 5-diol.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1278550A GB688553A (en) | 1950-05-22 | 1950-05-22 | Manufacture of glycols |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1278550A GB688553A (en) | 1950-05-22 | 1950-05-22 | Manufacture of glycols |
Publications (1)
Publication Number | Publication Date |
---|---|
GB688553A true GB688553A (en) | 1953-03-11 |
Family
ID=10011077
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1278550A Expired GB688553A (en) | 1950-05-22 | 1950-05-22 | Manufacture of glycols |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB688553A (en) |
-
1950
- 1950-05-22 GB GB1278550A patent/GB688553A/en not_active Expired
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