| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_e2dfabcff2df4f255715008a13853107
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a2a99738c564d0d4da77d442ec8f7500
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_0df7f1975ad6700746b5b2346b7b5d27
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_bca5beed8c36af4e54098bafe79fd13f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_e1539decc80f58b8877afe8bad7ca0d7 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1044
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-305 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G35-095
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G35-09
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G59-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G35-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G35-085
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G35-065 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G59-02 |
| filingDate |
2010-07-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4a79ff1b27e7b553f0d03d2a9d1d6ee7
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d492f665a3661e12d501d6e74a21c69f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c95bec704ee73dc8ffe2103fb25e8a5d
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c1031f1aab6f847da8d7fc0304c0e7e2 |
| publicationDate |
2012-02-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
US-2012024754-A1 |
| titleOfInvention |
Multi-stage reforming process with final stage catalyst regeneration |
| abstract |
The present invention relates to a multistage reforming process to produce a high octane product. A naphtha boiling range feedstock is processed in a multi-stage reforming process, in which said process involves at least 1) a penultimate stage for reforming the naphtha feedstock to produce a penultimate effluent 2) a final stage for further reforming at least a portion of the penultimate effluent 3) a regeneration step for the final stage catalyst. The severity of the penultimate stage can be increased during final stage catalyst regeneration in order to maintain the target RON of the reformate product and avoid reactor downtime. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2012260628-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2623434-C1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8889939-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11760941-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8763364-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8882992-B2 |
| priorityDate |
2010-07-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |