http://rdf.ncbi.nlm.nih.gov/pubchem/patent/GB-1180100-A
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_24aca9ded2638ea793d05360dde7a4a0 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-783 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-82 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-82 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-78 |
| filingDate | 1967-12-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 1970-02-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | GB-1180100-A |
| titleOfInvention | A process for Recovering Acrolein |
| abstract | 1,180,100. Recovery of acrolein. SUMITOMO CHEMICAL CO. Ltd. 27 Dec., 1967 [29 Dec., 1966], No. 58614/67. Heading C2C. Acrolein, in the form of an aqueous solution, is recovered from a gaseous reaction mixture obtained by gas phase catalytic oxidation of propylene by quenching, directly or indirectly, said reaction mixture down to a temperature of 30-80 C. to separate a condensate from the uncondensed vapour and then absorbing said uncondensed vapour into water at a temperature of 0-30 C. (after or while cooling the vapour to a temperature of 0-30 C.) to obtain an aqueous solution containing predominantly acrolein. In practice, the indirect quenching is effected by the use of cooling water or another suitable cooling medium and the direct quenching is effected by the use of the condensate itself after cooling. The condensate separated from the gaseous reaction mixture in the quenching step may either be discarded or subjected to distillation to recover the acrolein therefrom. The subsequent absorption stage is carried out after cooling the vapour indirectly either before or after the vapour enters the absorption column or directly by the use of the water for absorption, which is itself cooled so that the stated temperature range will be reached when the absorption of vapour occurs. The aqueous solution of acrolein is subsequently concentrated and purified by subjecting it to distillation, preferably under a pressure of 70 mm. Hg and at a temperature of - 1-53 C., and preferably by blowing steam into the distillate. Improved yields of pure acrolein are achieved if a small amount of polymerization inhibitor is added during the steam distillation. |
| priorityDate | 1966-12-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 17.