GB346221A - Process for the manufacture of acrolein - Google Patents
Process for the manufacture of acroleinInfo
- Publication number
- GB346221A GB346221A GB17816/30A GB1781630A GB346221A GB 346221 A GB346221 A GB 346221A GB 17816/30 A GB17816/30 A GB 17816/30A GB 1781630 A GB1781630 A GB 1781630A GB 346221 A GB346221 A GB 346221A
- Authority
- GB
- United Kingdom
- Prior art keywords
- phosphate
- acrolein
- glycerol
- pumice
- per cent
- 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
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/51—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition
- C07C45/52—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition by dehydration and rearrangement involving two hydroxy groups in the same molecule
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Acrolein is obtained by passing glycerol vapours at high temperatures, e.g. above 300 DEG C., over salts of acids which are higher than dibasic, or mixtures thereof. These salts may be distributed in metal tubes on carrier substances such as pumice, the impregnation of the carrier being effected by precipitation when necessary. By distillation from the receiver through a dephlegmator, pure acrolein is obtained, even when aqueous glycerol, e.g. 50 per cent glycerol, is sued as the starting material. In the examples, (1) pumice is impregnated with 1 per cent of normal lithium phosphate, dried, and introduced into a glass tube which is heated in an electric furnace to 400-420 DEG C. The product is fractionally distilled to yield acrolein. (2) Copper phosphate is employed at 425-430 DEG C. Further example of suitable catalysts, with their optimum temperatures, are bismuth phosphate (400 DEG C.), silver phosphate (400-410 DEG C.), ferric phosphate (390-410 DEG C.), and magnesium borate (500 DEG C.).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE346221X | 1929-06-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB346221A true GB346221A (en) | 1931-04-09 |
Family
ID=6255098
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB17816/30A Expired GB346221A (en) | 1929-06-15 | 1930-06-10 | Process for the manufacture of acrolein |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB346221A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2421554A (en) * | 1943-05-01 | 1947-06-03 | Shell Dev | Catalytic cleavage of glycols |
US8703450B2 (en) | 2005-02-28 | 2014-04-22 | Evonik Degussa Gmbh | Water-absorbent polymer structures based on renewable resources and method for producing said structures |
-
1930
- 1930-06-10 GB GB17816/30A patent/GB346221A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2421554A (en) * | 1943-05-01 | 1947-06-03 | Shell Dev | Catalytic cleavage of glycols |
US8703450B2 (en) | 2005-02-28 | 2014-04-22 | Evonik Degussa Gmbh | Water-absorbent polymer structures based on renewable resources and method for producing said structures |
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