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filingDate 1998-10-22-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_059085e4b267d8ee129241a33287a2d9
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publicationDate 2000-05-15-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-20000026638-A
titleOfInvention Catalyst for dehydrogenation reaction with macropores
abstract TECHNICAL FIELD The present invention relates to a catalyst to which an improved carrier having improved activity, selectivity and activity stability of a catalyst used for a dehydrogenation reaction of a saturated hydrocarbon gas having 5 or less carbon atoms is applied and which has a pore size of 1,000 Å or more, An alumina carrier having a pore size of at least 0.05 cc / g and a maximum of 0.5 cc / g and having a pore size distribution of at least 0.10 cc / g and a maximum of 0.9 cc / g or less with a distribution of 10-500 angstrom was applied, 0.05 to 2.0% by weight in terms of the elemental weight of the final catalyst, 0.05 to 1.0% by weight in terms of the elemental weight of tin (Sn) in the final catalyst, 0.05 to 3.0% by weight in terms of elemental weight in the alkali group 1 or 2 element, Is 0.0 to 2.0% by weight. The catalyst of the present invention has a large effect of improving the performance as the reaction conditions are severely taken to increase the yield of olefin, and there is little decrease in performance due to repetition of reaction and regeneration , It has strong physical stability.
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-101406563-B1
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priorityDate 1998-10-22-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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