http://rdf.ncbi.nlm.nih.gov/pubchem/patent/GB-464308-A
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7b04f5b6a02051c94d6eaf190b751ed2 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C1-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08G61-04 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C1-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G61-04 |
| filingDate | 1936-04-03^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 1937-04-15^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | GB-464308-A |
| titleOfInvention | Improvements in the production of hydrocarbons |
| abstract | <PICT:0464308/IV/1> In the conversion of carbon monoxide and hydrogen into hydrocarbons in presence of a rigidly arranged catalyst 1 a liquid supplied by a nozzle 4 is caused to trickle over the catalyst, to which the reaction gas is supplied by pipe 2. The liquid and the gaseous products are separated in the chamber 8 whereby the collection of a body of liquid in the reaction space is prevented. The liquid is preferably a solvent for the reaction products; examples are alcohols and middle, heavy, paraffin, and anthracene oils. The reaction products themselves may be employed if liquid. The conversion is effected at the usual temperatures namely 150--450 DEG C. and at reduced, atmospheric, or increased pressure.ALSO:<PICT:0464308/III/1> In the conversion of carbon monoxide and hydrogen into hydrocarbons in presence of a rigidly arranged catalyst, a liquid is caused to trickle over the catalyst while avoiding the formation of a body of liquid in the reaction space. The liquid is preferably a solvent for the reaction products; examples are alcohols, middle oils, heavy oils, paraffin oils, and anthracene oils. The reaction products themselves may be used if liquid under the working conditions. The conversion is effected at the usual temperatures, namely 150--450 DEG C. and at reduced, atmospheric, or increased pressure. The Figure shows a reaction chamber containing a catalyst 1 of iron with 5 per cent of alumina, which is sprinkled with liquid from the nozzle 4 while the reaction gas enters by pipe 2. The liquid and the gaseous products are separated in the chamber 8. |
| priorityDate | 1936-04-03^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
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