http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-5008666-B2
Outgoing Links
Predicate | Object |
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classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-0045 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1059 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-301 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-7815 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-48 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-202 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2229-42 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2229-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2229-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-64 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G11-05 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G11-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-002 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-0006 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G11-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-166 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G11-05 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J35-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-16 |
filingDate | 2007-06-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2012-08-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate | 2012-08-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | JP-5008666-B2 |
titleOfInvention | Desulfurization function-added fluid catalytic cracking catalyst, production method thereof, and method for producing low sulfur catalytic cracking gasoline using the desulfurization function-added fluid catalytic cracking catalyst |
abstract | The present invention 1, 2 or 3 provides a desulfurization function-added FCC catalyst which can efficiently reduce the sulfur content of FCC gasoline while maintaining the yield of FCC gasoline in a process of producing FCC gasoline by cracking of heavy oil. The catalyst has vanadium supported on a carrier comprising (a) an alumina-coated zeolite and (b) a porous inorganic oxide except zeolite and/or a clay mineral, wherein the supported vanadium amount is from 500 to 20000 ppm by mass in terms of vanadium metal and the acid amount is from 20 to 450 µmol/g and the macropore surface area is from 30 to 150 m 2 /g; or the catalyst has vanadium supported on a carrier containing from 5 to 40 % by mass of (a) an alumina-coated zeolite and from 30 to 70 % by mass of (b) an alumina, wherein the vanadium concentration ratio before and after grinding the catalyst is at least 2; or the catalyst has at least vanadium and manganese and/or phosphorus supported on a porous inorganic oxide-containing carrier, wherein the supported vanadium amount is from 500 to 20000 ppm by mass in terms of vanadium metal, vanadium and manganese and/or phosphorus form a complex ion in the supporting solution for use in supporting vanadium and manganese and/or phosphorus, and the permeability of the complex ion through a reverse osmosis membrane is at most 25 % relative to the permeability of vanadium through the reverse osmosis membrane. |
priorityDate | 2006-06-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 390.