http://rdf.ncbi.nlm.nih.gov/pubchem/patent/DE-2526035-A1

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classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C6-04
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C6-04
filingDate 1975-06-09-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8a16a4cfce91045ae53a9832eecb7dc8
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a9dc71645b7be55ca1cee78ae38dda39
publicationDate 1976-12-23-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber DE-2526035-A1
titleOfInvention METHOD OF DISPROPORTION OF PROPYLENE
abstract Propylene disproportionation, to ethylene and 2-butene, takes place in liq. phase with a Mo oxide-Al2O3 catalyst, at -40 to 100 degrees C, under standard press. to 200 kg/cm2. Novelty is carrying out process in a solvent consisting of paraffin, cycloparaffin, and/or aromatic hydrocarbons. Solvent : propylene vol. ratio is pref. 0.5 : 1 to 10 : 1. Side-reactions, e.g. polymerisation or isomerisation of 2-butene and catalyst deactivation by polymers, are prevented. Solvents easily dissolve any polymers and oligomers formed and remove them from catalyst surface. Process can be carried out for a long time at 100 degrees C and yields ethylene and 2-butene at constant rates. Solvents can be recoverd and re-used. Reaction velocity, catalyst activity and selectivity are improved. E.g. use of n-heptane in vol. ratio solvent/ C3H6 = 4 at LHSV 50, 80 degrees C, 50 atmos., improved max. C3H6 conversion from 25- to 46%, selectivity to ethylene and butene from 95- to 99% and ratio butene/ethylene from 1.65 to 0.995.
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priorityDate 1975-06-09-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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