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公开(公告)号：EP1137739B1
公开(公告)日：2004-03-17
申请号：EP00904469.4
申请日：2000-01-21
发明人： CHESTER, Arthur, Warren , GREEN, Larry, Arthur , DHINGRA, Sandeep, Singh , MASON, Timothy , TIMKEN, Hye, Kyung, Cho
CPC分类号： C07C6/126 , B01J29/04 , B01J29/70 , C01B39/085 , C01B39/48 , C07C2/66 , C07C4/18 , C07C5/2708 , C07C6/123 , C07C2529/70 , C07C15/02 , C07C15/00
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公开(公告)号：EP1153105A1
公开(公告)日：2001-11-14
申请号：EP99965275.3
申请日：1999-12-16
IPC分类号： C10G35/04 , C10G35/095 , C07C2/64 , C07C2/66
CPC分类号： C10G29/205
摘要： A process of increasing the cetane index of a distillate pool comprising contacting a first refinery-grade feedstream of an aromatic compounds-containing heavy gasoline or distillate fuel feedstream with a second refinery-grade feedstream containing olefins in the presence of an acidic solid alkylation catalyst under alkylation conditions, wherein both the aromatic-containing feedstream and the olefin-containing feedstream are simultaneously upgraded to suitable fuel products without addition of hydrogen.
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公开(公告)号：EP1220881B1
公开(公告)日：2005-07-27
申请号：EP00965178.7
申请日：2000-09-20
发明人： BHORE, Nazeer, A. , CHESTER, Arthur, W. , LIU, Ke , TIMKEN, Hye, Kyung, Cho , CHENG Wu-Cheng , KUMAR Ranjit , ZIEBARTH Michael Scott
CPC分类号： C10G11/05 , C10G11/02 , C10G11/18 , C10G2300/202 , C10G2300/4093 , C10G2300/70 , C10G2300/80 , C10G2400/02 , C10L1/06
摘要： The sulphur content of liquid cracking products, especially the cracked gasoline, of the catalytic cracking process is reduced by the use of a sulphur reduction additive comprising a non-molecular sieve support containing a high content of vanadium. Preferably, the support is alumina. The sulfur reduction is used in the form of a separate particle additive in combination with the active catalytic cracking catalyst (normally a faujasite such as zeolite Y) to process hydrocarbon feedstocks in the fluid catalytic cracking (FCC) unit to produce low-sulfur gasoline and other liquid products.
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4.发明公开A CATALYTIC CRACKING PROCESS USING A MODIFIED MESOPOROUS ALUMINOPHOSPHATE MATERIAL 审中-公开催化裂化过程中使用的介孔磷酸铝
公开(公告)号：EP1255802A1
公开(公告)日：2002-11-13
申请号：EP00984409.3
申请日：2000-12-15
发明人： CHESTER, Arthur, W. , DAUGHERTY, Frederick, E. , FUNG, Anthony, S. , KRESGE, Charles, T. , TIMKEN, Hye, Kyung, Cho , VARTULI, James, C. , KUMAR, Ranjit , ROBERIE, Terry, G. , ZIEBARTH, Michael, S.
CPC分类号： C10G11/05
摘要： A process for catalytic cracking of a hydrocarbon feedstock comprises contacting the feedstock with a catalyst composition comprising a primary cracking component, such as zeolite Y, and a mesoporous aluminophosphate material which includes a solid aluminophosphate composition modified with at least one element selected from zirconium, cerium, lanthanum, manganese, cobalt, zinc, and vanadium. The mesoporous aluminophosphate material has a specific surface area of at least 100 m2/g, an average pore size less than or equal to 100 Å, and a pore size distribution such that at least 50 % of the pores have a pore diameter less than 100 Å.
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公开(公告)号：EP0781315B1
公开(公告)日：2001-10-31
申请号：EP95929542.9
申请日：1995-08-15
CPC分类号： C10G69/08 , C10G35/095
摘要： Low sulfur gasoline of relatively high octane number is produced from a cracked, sulfur-containing olefinic naphthas by hydrodesulfurization followed by treatment over an acidic catalyst comprising an intermediate pore size zeolite such as zeolite ZSM-5 in combination with molybdenum. The use of the molybdenum in combination with the zeolite has been found to give improved catalytic activity coupled with lower coking, longer catalyst life and other advantages.
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公开(公告)号：EP0783557B1
公开(公告)日：2004-08-11
申请号：EP95935228.7
申请日：1995-09-27
发明人： BUCHANAN, John, Scott , CHENG, Jane, Chi-Ya , HAAG, Werner, Otto , HARANDI, Mohsen, Nadimi , MORRISON, Roger, Allan , FREYMAN, David, George , MAZZONE, Dominick, Nicholas , ROULEAU, Norman, Joseph , SORENSEN, Charles, Mitchel , TIMKEN, Hye, Kyung, Cho , WARE, Robert, Adams
IPC分类号： C10G35/085 , C10G35/095 , C10G59/02 , C10G69/08
摘要： This is a process for upgrading a petroleum naphtha fraction. The naphtha (10) is subjected to reforming (16a, 16b, 16c) and the reformate is cascaded to a benzene and toluene synthesis zone (18) over a synthesis catalyst comprising a molecular sieve of low acid activity. The preferred molecular sieve is steamed ZSM-5. The benzene and toluene synthesis zone (18) is operated under conditions compatible with the conditions of the reformer such as pressures of above about 50 psig (446 kPa) and temperatures above about 800 DEG F (427 DEG C). In one aspect of the invention, the benzene and toluene synthesis catalyst includes a metal hydrogenation component such as cobalt, nickel, platinum and palladium. In one mode of operation, the benzene and toluene synthesis catalyst replaces at least a portion of the catalyst of the reformer. The process produces a product containing an increased proportion of benzene and toluene, and reduced proportion of C8 aromatics, particularly ethylbenzenes, as compared to the reformate.
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公开(公告)号：EP0701596B1
公开(公告)日：2002-07-31
申请号：EP94916760.5
申请日：1994-05-16
CPC分类号： C10G47/16 , B01J29/084 , B01J29/70
摘要： In a process for preparing an alumina bound, zeolite catalyst, a zeolite of low silanol content is used as the source of zeolite used to prepare the catalyst. A particular zeolite used in this catalyst is zeolite Y. This catalyst may be combined with at least one hydrogenation component and used to hydrocrack hydrocarbons, such as gas oils. In particular, an NiW/USY/alumina catalyst may be used in a hydrocracking reaction to produce distillate boiling range hydrocarbons from higher boiling hydrocarbons.
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