| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_75a9b43328a2cbfcf60da8b223a321c7 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00061
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y10S585-91
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-0007
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-0053
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00504
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00495
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00407
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00194 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2-84
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2-82 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C9-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-34
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G50-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C2-82
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C2-84
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G57-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C67-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C1-00 |
| filingDate |
1988-03-25^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0534bd137e9ed041b50d597fa38a304a
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b9c41d7a141430113e7d186a4b62b8bc |
| publicationDate |
1988-10-05^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
EP-0285337-A1 |
| titleOfInvention |
Thin bed reactors for methane conversion |
| abstract |
Methane is converted to higher hydrocarbons by reaction with a gaseous oxidant under adiabatic conditions in a thin bed reactor, the feed being supplied to the reactor at a temperature of at least 100°C below reaction temperature and being heated to reaction temperature by conductive flow of heat generated by the reaction axially through the bed countercurrent to feed flow. A suitable reactor has a preheat zone and a reaction zone with axial flow of reaction heat from the reaction zone to the preheat zone. |
| priorityDate |
1987-03-30^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |