http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-100995088-B1

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classificationCPCAdditional http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2521-12
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-52
classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C11-06
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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C2-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00
filingDate 2008-08-14-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2010-11-18-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationDate 2010-11-18-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-100995088-B1
titleOfInvention Process for producing high selectivity propylene from methanol or dimethyl ether using crystalline H-FE-WSM-5 catalyst
abstract The present invention relates to a process for producing high selectivity propylene from methanol or dimethyl ether using crystalline H-Fe-ZSM-5 catalyst. More specifically, the iron (Fe) component is introduced into the zeolite (H-ZSM-5) framework into a mixture of methanol or dimethyl ether and a diluent gas as a reactant, thereby introducing silicon (Si) and aluminum (Al). Crystalline H-Fe-ZSM-5 catalyst consisting of iron (Fe) and oxygen (O) is introduced into the conversion of methanol or dimethyl ether to a process for producing highly selective propylene.n n n In the present invention, when the mixture containing methanol or dimethyl ether and diluent gas is converted, the propylene / ethylene (C 3 = / C 2 =) ratio is high, and the propane / propylene (C 3 / C 3 =) ratio is low. Mixtures can be prepared. The volume ratio of feedstock and diluent gas in the reactant is 1: 100 to 5: 1.n n n n Propylene, Methanol, Dimethyl Ether, Zeolite, H-Fe-ZSM-5
priorityDate 2008-08-14-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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Total number of triples: 42.