http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-103752319-B

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Predicate Object
classificationCPCAdditional http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-52
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B3-40
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-835
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-83
filingDate 2013-12-31-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2016-08-17-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationDate 2016-08-17-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-103752319-B
titleOfInvention Anti-carbon Ni methylmethane vapor reforming hydrogen production catalyst and preparation method thereof
abstract The present invention relates to a kind of catalyst for hydrogen production from methane vapor reforming and preparation method thereof, using Lanthanum (III) nitrate, praseodymium nitrate, samaric nitrate, Yttrium trinitrate and zirconium nitrate, zirconium carbonate, zirconium oxychloride etc. is presoma, with ammonia as precipitant, prepare pyrochlore composite oxides by coprecipitation method, then utilize the method for mechanical mixture to be combined with aluminium oxide and prepare pyrochlore alumina composite carrier.Direct impregnation is used to load on pyrochlore alumina composite carrier with nickel nitrate, Nickel dichloride., nickel sulfate, nickel oxalate etc. for nickel source.In catalyst, the load capacity of nickel is the 5 ~ 30% of catalyst weight, and the content of pyrochlore is the 5 ~ 50% of catalyst, the content of aluminium oxide be the ratio of catalyst be 20 ~ 90%.Utilize pyrochlore alumina composite oxide can improve reactivity and the anti-carbon performance of catalyst greatly as carrier, and method for preparing catalyst is simple, methane vapor reforming is had excellent catalysis activity and stability by fixed bed.
priorityDate 2013-12-31-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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