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1. (WO2013148397) CATALYST FOR CONVERSION OF HYDROCARBONS
Latest bibliographic data on file with the International Bureau   

Pub. No.: WO/2013/148397 International Application No.: PCT/US2013/032792
Publication Date: 03.10.2013 International Filing Date: 18.03.2013
IPC:
B01J 23/63 (2006.01) ,B01J 23/58 (2006.01) ,C10G 35/09 (2006.01) ,C10G 59/02 (2006.01)
B PERFORMING OPERATIONS; TRANSPORTING
01
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
J
CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
23
Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/113
38
of noble metals
54
combined with metals, oxides or hydroxides provided for in groups B01J23/02-B01J23/36118
56
Platinum group metals
63
with rare earths or actinides
B PERFORMING OPERATIONS; TRANSPORTING
01
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
J
CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
23
Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/113
38
of noble metals
54
combined with metals, oxides or hydroxides provided for in groups B01J23/02-B01J23/36118
56
Platinum group metals
58
with alkali- or alkaline earth metals or beryllium
C CHEMISTRY; METALLURGY
10
PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
G
CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
35
Reforming naphtha
04
Catalytic reforming
06
characterised by the catalyst used
085
containing platinum group metals or compounds thereof
09
Bimetallic catalysts in which at least one of the metals is a platinum-group metal
C CHEMISTRY; METALLURGY
10
PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
G
CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
59
Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
02
plural serial stages only
Applicants:
UOP LLC [US/US]; 25 East Algonquin Road P. O. Box 5017 Des Plaines, Illinois 60017-5017, US
Inventors:
SERBAN, Manuela; US
LAPINSKI, Mark P.; US
Agent:
GOLDBERG, Mark; UOP LLC 25 East Algonquin Road P. O. Box 5017 Des Plaines, Illinois 60017-5017, US
Priority Data:
13/547,35112.07.2012US
61/617,20129.03.2012US
Title (EN) CATALYST FOR CONVERSION OF HYDROCARBONS
(FR) CATALYSEUR POUR LA CONVERSION D'HYDROCARBURES
Abstract:
(EN) One embodiment is a catalyst for catalytic reforming of naphtha. The catalyst can have a noble metal including one or more of platinum, palladium, rhodium, ruthenium, osmium, and iridium, an alkali or alkaline-earth metal, a lanthanide-series metal, and a support. Generally, an average bulk density of the catalyst is 0.300 to 1.00 gram per cubic centimeter. The catalyst has a platinum content of less than 0.375 wt%, a tin content of 0.1 to 2 wt%, a potassium content of 100 to 600 wppm, and a cerium content of 0.1 to 1 wt%. The lanthanide-series metal can be distributed at a concentration of the lanthanide-series metal in a 100 micron surface layer of the catalyst less than two times a concentration of the lanthanide-series metal at a central core of the catalyst.
(FR) Selon un mode de réalisation, l'invention porte sur un catalyseur pour le reformage catalytique de naphta. Le catalyseur peut comporter un métal noble comprenant un ou plusieurs métaux nobles, choisis parmi le platine, le palladium, le rhodium, le ruthénium, l'osmium et l'iridium, un métal alcalin ou alcalinoterreux, un métal de la série des lanthanides et un support. En général, la masse volumique apparente moyenne du catalyseur est de 0,300 à 1,00 gramme par centimètre cube. Le catalyseur présente une teneur en platine inférieure à 0,375 % en poids, une teneur en étain de 0,1 à 2 % en poids, une teneur en potassium de 100 à 600 ppm en poids et une teneur en cérium de 0,1 à 1 % en poids. Le métal de la série des lanthanides peut être réparti en une concentration du métal de la série des lanthanides inférieure, dans une couche de surface de 100 micromètres du catalyseur, à deux fois une concentration du métal de la série des lanthanides au niveau d'une partie centrale du catalyseur.
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Designated States: AE, AG, AL, AM, AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, BZ, CA, CH, CL, CN, CO, CR, CU, CZ, DE, DK, DM, DO, DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, HN, HR, HU, ID, IL, IN, IS, JP, KE, KG, KM, KN, KP, KR, KZ, LA, LC, LK, LR, LS, LT, LU, LY, MA, MD, ME, MG, MK, MN, MW, MX, MY, MZ, NA, NG, NI, NO, NZ, OM, PA, PE, PG, PH, PL, PT, QA, RO, RS, RU, RW, SC, SD, SE, SG, SK, SL, SM, ST, SV, SY, TH, TJ, TM, TN, TR, TT, TZ, UA, UG, US, UZ, VC, VN, ZA, ZM, ZW
African Regional Intellectual Property Organization (ARIPO) (BW, GH, GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, SZ, TZ, UG, ZM, ZW)
Eurasian Patent Office (AM, AZ, BY, KG, KZ, RU, TJ, TM)
European Patent Office (EPO) (AL, AT, BE, BG, CH, CY, CZ, DE, DK, EE, ES, FI, FR, GB, GR, HR, HU, IE, IS, IT, LT, LU, LV, MC, MK, MT, NL, NO, PL, PT, RO, RS, SE, SI, SK, SM, TR)
African Intellectual Property Organization (BF, BJ, CF, CG, CI, CM, GA, GN, GQ, GW, ML, MR, NE, SN, TD, TG)
Publication Language: English (EN)
Filing Language: English (EN)