GB773436A - Improvements in or relating to the preparation of polyhydric alcohols - Google Patents
Improvements in or relating to the preparation of polyhydric alcoholsInfo
- Publication number
- GB773436A GB773436A GB16203/55A GB1620355A GB773436A GB 773436 A GB773436 A GB 773436A GB 16203/55 A GB16203/55 A GB 16203/55A GB 1620355 A GB1620355 A GB 1620355A GB 773436 A GB773436 A GB 773436A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reaction
- yields
- methyl
- chloro
- temperatures
- 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
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/34—Halogenated alcohols
- C07C31/36—Halogenated alcohols the halogen not being fluorine
-
- 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
- C07C29/62—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by introduction of halogen; by substitution of halogen atoms by other halogen atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D301/00—Preparation of oxiranes
- C07D301/02—Synthesis of the oxirane ring
- C07D301/24—Synthesis of the oxirane ring by splitting off HAL—Y from compounds containing the radical HAL—C—C—OY
- C07D301/26—Y being hydrogen
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Polyhydric alcohols are prepared by passing aqueous halohydrins and inorganic basic hydrolysing agents through a plurality of reaction stages maintained at hydrolysing temperatures above 25 DEG C., the mixture introduced into the first stage containing only a substantial part of the total stoichiometric requirement of basic agents for the hydrolysis, and additional amounts of basic agent being introduced at one or more subsequent reaction stages in such a manner that the pH value of the reaction mixture is maintained at between 8 and 10 throughout the reaction. Temperatures between 75 DEG C. and 250 DEG C. are generally suitable for carrying out the process. In operations at temperatures in the range of about 75 DEG C. to about 110 DEG C. the reaction may be carried out at atmospheric pressure, but at higher temperatures it is preferred to carry out the reaction under super-atmospheric pressure, provided preferably by carbon dioxide under pressure. The reaction is preferably carried out with a total amount of base which is at least equivalent to the halogen in the starting halohydrin. Generally about 2 to 15 per cent excess of basic agent is used. The basic agent is divided among the different reaction stages in the proportions required to maintain the reaction mixture therein at the required pH value. Suitable inorganic bases are, for example, alkali metal hydroxides, carbonates, phosphates, polyphosphates or borates. The halohydrins used as starting materials may be substituted by aromatic or cycloaliphatic groups. In the examples: (a) epichlorhydrin containing about 25 per cent by weight of dichlorhydrins is hydrolysed in a vessel divided into five compartments by injecting the epichlorhydrin mixed with sodium carbonate solution into the first compartment and adding sodium hydroxide to subsequent compartments so that the pH is maintained at the value 9.6; glycerin is separated from the reaction mixture; (b) similarly 1-chloro-2.3-epoxy butane yields 1.2.3-trihydroxybutane, p-methyl epichlorhydrin yields b -methyl glycerin, ethylene and propylene chlorohydrin yield ethylene and propylene glycol respectively, 1-chloro-2.3-dihydroxybutane and 2-chloro - 1.3 - dihydroxybutane yield a - methyl glycerine, 1 - chloro - 2 - methyl - 2.3 - dihydroxybutane yields b -methyl glycerine, 1-bromo-3.4-dihydroxypetane yields 1.3.4-trihydroxy-pentane and 1.4-dihydroxy-5-chlorodecane yields 3.4.5-trihydroxydecane. Specification 569,717, [Group IV], is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US773436XA | 1954-06-07 | 1954-06-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB773436A true GB773436A (en) | 1957-04-24 |
Family
ID=22137504
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB16203/55A Expired GB773436A (en) | 1954-06-07 | 1955-06-06 | Improvements in or relating to the preparation of polyhydric alcohols |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB773436A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2748799A1 (en) * | 1976-11-01 | 1978-05-03 | Shell Int Research | PROCESS FOR PRODUCING GLYCERIN |
-
1955
- 1955-06-06 GB GB16203/55A patent/GB773436A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2748799A1 (en) * | 1976-11-01 | 1978-05-03 | Shell Int Research | PROCESS FOR PRODUCING GLYCERIN |
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