http://rdf.ncbi.nlm.nih.gov/pubchem/patent/GB-271523-A
Outgoing Links
Predicate | Object |
---|---|
assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_fad2b1bdf7ec880532f58d8f1c39b90d |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B3-16 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B3-16 |
filingDate | 1927-05-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate | 1928-06-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | GB-271523-A |
titleOfInvention | Catalytic process for the manufacture of hydrogen |
abstract | 271,523. Grenier, R. J. A. May 22, 1926, [Convention date]. Methyl alcohol.-The reaction between carbon monoxide and steam for the production of hydrogen is effected with the use as catalyst of carbon in the porous state; the preferred catalyst is wood charcoal. For example, the production of hydrogen may be effected by passing carbon monoxide, or gases, such as water gas, poor gas, or coke oven gas, containing carbon monoxide, admixed with steam through a gas-heated iron tube filled with wood charcoal. The reaction may be effected under pressure and at a temperature of 350‹ C. The Specification as open to inspection under Sect. 91 (3) (a) states that other reactions in which carbon monoxide takes part, such as the production of methyl alcohol from carbon monoxide and hydrogen are effected in a similar manner. This subject-matter does not appear in the Specification as accepted. |
priorityDate | 1926-05-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 24.