http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-0418370-A4
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-584 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2529-40 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2-66 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C2-70 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C2-66 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C15-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G35-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G35-06 |
| filingDate | 1990-03-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 1991-09-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | EP-0418370-A4 |
| titleOfInvention | Process for the production of alkyl aromatic hydrocarbons |
| abstract | A process for the production of gasoline from a C4-fuel gas containing ethene and propene and catalytic reformate containing C6 to C8 aromatic hydrocarbons. The C4-fuel gas in stream (28) is obtained by catalytic cracking of the vacuum gas oil fraction (7) obtained by distillation of a crude feed (1) in a distillation apparatus (2). The reformate C6-C8 aromatic hydrocarbons in stream (15) is obtained by hydrotreating naphta (5) in zone (9), followed by reforming in zone (13). The C4-fuel gas (28) and C6-C8 aromatic reformate (15) are mixed and contacted in a catalytic reactor (29) with a zeolite catalyst to convert ethene and propene in the fuel gas to C5+ aliphatic and aromatic hydrocarbon gasoline and to convert C6 to C8 aromatics in the reformate into C7 to C11 hydrocarbon gasoline. In a preferred embodiment, the process comprises maintaining a fluidized bed of zeolite catalyst particles in a turbulent reactor be at a temperature of 350-900 DEG C and a pressure of 20-650 psig (240-4580 kpa). The weight ratio or aromatics to olefins is at least 5:1. |
| priorityDate | 1989-03-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 41.