GB793766A - Preparation of alkylene glycols - Google Patents
Preparation of alkylene glycolsInfo
- Publication number
- GB793766A GB793766A GB31184/56A GB3118456A GB793766A GB 793766 A GB793766 A GB 793766A GB 31184/56 A GB31184/56 A GB 31184/56A GB 3118456 A GB3118456 A GB 3118456A GB 793766 A GB793766 A GB 793766A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- copper
- phosphate
- mixture
- glycols
- 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
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/09—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis
- C07C29/10—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes
- C07C29/103—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes of cyclic ethers
- C07C29/106—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes of cyclic ethers of oxiranes
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
Glycols are obtained from C2-C4 alkylene oxides (having the oxygen atom attached to adjacent carbon atoms) by passing the vapour with more than an equimolar proportion of water over a catalyst comprising a normal calcium phosphate below 500 DEG C. Preferably more than 6 equivalents of water are used, and desirably more than 17 if the reactor has a stationary bed of catalyst. The reaction temperature may be 200-400 DEG C., e.g. 275-325 DEG C. the contact time being 1-25 seconds for a temperature of 250-350 DEG C. when the mixture is passed through a fluid bed of catalyst. The latter should consist preponderantly of tricalcium phosphate, promoted if desired with copper phosphate. A suitable catalyst is composed of Ca3(PO4)2 and CaHPO4 with a mol. ratio CaO/P2O5 of 2.7-2.8 and containing 0.1-1 per cent of copper. The vapour issuing from the catalyst is condensed to give a strong aqueous solution of glycol containing very little polyglycols. Examples are given of the production of ethylene glycol and it is stated that 1:2-propylene glycol and 1:2- and 2:3-butylene glycols may also be obtained from the corresponding alkylene oxides.ALSO:A catalyst for the vapour phase hydration of alkylene oxides to glycols consists essentially of a normal calcium phosphate, promoted if desired with copper. A suitable catalyst is composed of Ca3(PO4)2 and CaHPO4 with a mol. ratio CaO/P2O4 of 2.7-2.8 and containing 0.1-1.0 per cent of copper, e.g. as phosphate. Such a mixture can be obtained by adding phosphoric acid and ammonia (or other alkali) to a solution of calcium and copper chlorides, separating, washing and drying the precipitate. It may if desired be mixed in powdered or granular form with a lubricant, such as graphite, and pressed into tablets, the lubricant then being removed by oxidation. The catalyst may also be made by grinding together an aqueous mixture of calcium and copper phosphates and drying the resultant mixture.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB31184/56A GB793766A (en) | 1956-10-12 | 1956-10-12 | Preparation of alkylene glycols |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB31184/56A GB793766A (en) | 1956-10-12 | 1956-10-12 | Preparation of alkylene glycols |
Publications (1)
Publication Number | Publication Date |
---|---|
GB793766A true GB793766A (en) | 1958-04-23 |
Family
ID=10319258
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB31184/56A Expired GB793766A (en) | 1956-10-12 | 1956-10-12 | Preparation of alkylene glycols |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB793766A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8309771B2 (en) | 2008-08-05 | 2012-11-13 | Dow Technology Investments Llc | Two-stage, gas phase process for the manufacture of alkylene glycol |
-
1956
- 1956-10-12 GB GB31184/56A patent/GB793766A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8309771B2 (en) | 2008-08-05 | 2012-11-13 | Dow Technology Investments Llc | Two-stage, gas phase process for the manufacture of alkylene glycol |
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