GB686254A - Improvements in or relating to the manufacture of pentaerythritols - Google Patents
Improvements in or relating to the manufacture of pentaerythritolsInfo
- Publication number
- GB686254A GB686254A GB885150A GB885150A GB686254A GB 686254 A GB686254 A GB 686254A GB 885150 A GB885150 A GB 885150A GB 885150 A GB885150 A GB 885150A GB 686254 A GB686254 A GB 686254A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquor
- pentaerythritols
- condensation
- cation
- sulphate
- 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
- C07C31/18—Polyhydroxylic acyclic alcohols
- C07C31/24—Tetrahydroxylic alcohols, e.g. pentaerythritol
- C07C31/245—Pentaerythritol
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Pentaerythritols are made by condensing formaldehyde and acetaldehyde in aqueous solution with a strong alkaline earth base and precipitating and mechanically removing at the end of the condensation part of the alkaline earth metals present in solution, passing the resultant liquor through a bed of cation-exchange material to replace the residual alkaline earth ions by hydrogen ions, and eventually subjecting the thus treated liquor to flash evaporation. "Pentaerythritols" is defined as pentaerythritol in admixture with dipentaerythritol and other polypentaerythritols that accompany it as by-products of the above condensation. Lime is the specified base. Flash evaporation may be effected on hot rolls in vacuo or by spraying into a non-oxidizing gas. Preferably the liquor is concentrated before evaporation. A crop of pentaerythritol may be recovered before the evaporation. Preferably before cation exchange treatment liquor from the condensation is treated with sulphuric acid to precipitate calcium ions which are mechanically removed as the sulphate then with a barium salt, e.g. the carbonate, in an equivalent amount to the excess sulphate present and barium sulphate removed. After cation - exchange treatment any formic acid present may be neutralized with ammonia before concentration and flashing or the liquor may be passed through anion exchange material to reduce or remove residual sulphuric and formic acid. Preferably cation exchange treatment is effected when the liquor is dilute and before pentaerythritols are recovered. Preferably the condensation is effected so that no rise in temperature occurs towards the end of the addition of the reagents. "Zeo-carb" 215 (Registered Trade Mark) and Deacidite E are specified cation and anion exchange materials respectively. On washing the pentaerythritols with cold water they are obtained substantially free from syrupy formaldehyde products. In an example liquor from the condensation is treated with formic acid to dissolve excess lime, steam distilled to recover formaldehyde, sulphuric acid added and calcium sulphate filtered off, barium carbonate added and barium sulphate removed, the filtrate run through "Zeo-carb" 215 and the liquor concentrated to 1/4 of its volume and dried by spray drying into air.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB885150A GB686254A (en) | 1950-04-11 | 1950-04-11 | Improvements in or relating to the manufacture of pentaerythritols |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB885150A GB686254A (en) | 1950-04-11 | 1950-04-11 | Improvements in or relating to the manufacture of pentaerythritols |
Publications (1)
Publication Number | Publication Date |
---|---|
GB686254A true GB686254A (en) | 1953-01-21 |
Family
ID=9860457
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB885150A Expired GB686254A (en) | 1950-04-11 | 1950-04-11 | Improvements in or relating to the manufacture of pentaerythritols |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB686254A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3076854A (en) * | 1955-12-05 | 1963-02-05 | Heyden Newport Chemical Corp | Recovery of trimethylolpropane |
EP0012907A1 (en) * | 1978-12-20 | 1980-07-09 | Bayer Ag | Process for the purification of low molecular weight polyhydroxy compounds |
CN114276214A (en) * | 2021-12-10 | 2022-04-05 | 湖北宜化化工股份有限公司宜都分公司 | Production method for producing pentaerythritol by recycling carbide slag |
-
1950
- 1950-04-11 GB GB885150A patent/GB686254A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3076854A (en) * | 1955-12-05 | 1963-02-05 | Heyden Newport Chemical Corp | Recovery of trimethylolpropane |
EP0012907A1 (en) * | 1978-12-20 | 1980-07-09 | Bayer Ag | Process for the purification of low molecular weight polyhydroxy compounds |
CN114276214A (en) * | 2021-12-10 | 2022-04-05 | 湖北宜化化工股份有限公司宜都分公司 | Production method for producing pentaerythritol by recycling carbide slag |
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