Chiyoda Chemical Engineering & Construction Co., Ltd. (Yokohama JPX 03)
인용정보
피인용 횟수 :
60인용 특허 :
5
초록▼
A catalyst for hydrocracking heavy hydrocarbon oils includes a porous inorganic carrier composed mainly of alumina or titania, and two or more catalytic metal components composited with the carrier. The metals of the catalytic metal components are either (a) V and at least one element selected from
A catalyst for hydrocracking heavy hydrocarbon oils includes a porous inorganic carrier composed mainly of alumina or titania, and two or more catalytic metal components composited with the carrier. The metals of the catalytic metal components are either (a) V and at least one element selected from Zn, Fe, Co, Ni, Cu, Ag, Sn and Pb or (b) Mo and at least one element selected from Zn, Cu, Ag, Sn, Pb and the lanthanum-series elements. The catalyst has at least 60% of its total pore volume in pores with a diameter of 200 Åor more, at least 40% of its totalpore volume in pores with a diameter of 300 Åor more and not more than 20% of its total pore volume in pores with a diameter of at least 1000 Å. Disclosed also is a process for hydrocracking a heavy hydrocarbon oil in the presence of the above catalyst.
대표청구항▼
A catalyst for hydrocracking heavy hydrocarbon oils, comprising: a porous inorganic carrier composed mainly of alumina or titania; and two or more catalytic metal components composited with said carrier, the metals of said catalytic metal components being either (a) V and at least one first auxiliar
A catalyst for hydrocracking heavy hydrocarbon oils, comprising: a porous inorganic carrier composed mainly of alumina or titania; and two or more catalytic metal components composited with said carrier, the metals of said catalytic metal components being either (a) V and at least one first auxiliary element selected from the group consisting of Zn, Fe, Co, Ni, Cu, Ag, Sn and Pb or (b) Mo and at least one second auxiliary element selected from the group consisting of Zn, Cu, Ag, Sn, Pb and the lanthanum-series elements, said catalyst having at least 60% of its total pore volume in pores with a diameter of 200 Åor more, at least 40% of its total pore volume in pores with a diameter of 300 Åor more and not more than 20% of its total pore volume in pores with a diameter of at least 1000 Å. A process for hydrocracking a heavy hydrocarbon oil, comprising contacting the heavy hydrocarbon oil with a catalyst at a temperature of 420°-480°C., a hydrogen pressure of 100-250 Kg/cm2 and a liquid hourly space velocity of 0.1-10 hr-1, said catalyst including a porous inorganic carrier composed mainly of alumina or titania, and two or more catalytic metal components composed with said carrier, the metals of said catalytic metal components being either (a) V and at least one first auxiliary element selected from the group consisting of Zn, Fe, Co, Ni, Cu, Ag, Sn and Pb or (b) Mo and at least one second auxiliary metal component selected from the group consisting of Zn, Cu, Ag, Sn, Pb and the lanthanum-series elements, and said catalyst having at least 60% of its total pore volume in pores with a diameter of 200 Åor more, at least 40% of its total pore volume in pores with a diameter of 300 Åor more and not more than 20% of its total volume in pores with a diameter of at least 1000 Å.
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이 특허에 인용된 특허 (5)
Le Page Jean-Francois (Rueil Malmaison FRX) Billon Alain (Orlienas FRX) Jacquin Yves (Sevres FRX), Catalyst and process for hydrorefining hydrocarbon charges with high contents of metals, resins and/or asphaltenes.
Eastman Alan D. (Bartlesville OK) Gardner Lloyd E. (Bartlesville OK), Catalytic hydrodesulfurization or hydrodenitrogenation of organic compounds employing alumina promoted with zinc, titani.
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Coombs Daniel M. (Borger TX) Nowack Gerhard P. (Bartlesville OK) Bertus Brent J. (Bartlesville OK) Kukes Simon G. (Bartlesville OK), Hydrodemetallization of oils.
Parrott Stephen L. (Bartlesville OK) Kukes Simon G. (Bartlesville OK) Brandes Karlheinz K. (Bartlesville OK), Hydrofining catalyst composition and process for its preparation.
Wallace, Andrew P.; Melack, John M.; Lefenfeld, Michael, Hydrogen generation systems and methods utilizing sodium silicide and sodium silica gel materials.
Wallace, Andrew P.; Melack, John M.; Lefenfeld, Michael, Hydrogen generation systems and methods utilizing sodium silicide and sodium silica gel materials.
Lefenfeld, Michael; Dye, James L.; Nandi, Partha; Jackson, James, Lithium-porous metal oxide compositions and lithium reagent-porous metal compositions.
Bogdan, Paula L.; Nemeth, Valeria J.; Bare, Simon R., Method of making substantially nonporous substrate supported noble metal- and lanthanide-containing catalysts.
Morales Alfredo (Caracas VEX) Galiasso Roberto (Caracas VEX) Carrasquel Angel R. (Caracas VEX), Process for catalyst preparation for the hydrodemetallization of heavy crudes and residues.
Calemma, Vincenzo; Flego, Cristina; Carluccio, Luciano Cosimo; Parker, Wallace; Giardino, Roberto; Faraci, Giovanni, Process for the preparation of middle distillates and lube bases starting from synthetic hydrocarbon feedstocks.
Bogdan, Paula L.; Nemeth, Valeria J.; Bare, Simon R., Substantially nonporous substrate supported noble metal- and lanthanide-containing catalysts for hydrogenation reactions.
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