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1.
公开(公告)号:EP1689677B1
公开(公告)日:2010-08-18
申请号:EP04798035.4
申请日:2004-11-19
发明人: LAHEIJ, Erik, Jeroen , O'CONNOR, Paul , STAMIRES, Dennis , MORGADO JUNIOR, Edisson , SANTOS DE ABREU, Marco, Antonio , FERNANDES, Márcio , BRADY, Michael
CPC分类号: C04B35/6303 , B82Y30/00 , C01F7/02 , C01F7/34 , C01F7/448 , C01P2002/04 , C01P2002/70 , C01P2004/62 , C01P2004/64 , C04B35/62605 , C04B35/63 , C04B2235/3218 , C04B2235/5454 , C04B2235/549
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公开(公告)号:EP1363725B1
公开(公告)日:2004-11-03
申请号:EP02718147.8
申请日:2002-02-15
发明人: LAM, Yiu, Lau , DA SILVA SANTOS, Anselmo , RONCOLATTO, Rodolfo, Eugênio , TOREM, Marcelo, André , MORGADO JUNIOR, Edisson , O'CONNOR, Paul
IPC分类号: B01J2/00
CPC分类号: B01J29/088 , B01J35/0006 , B01J35/10 , B01J35/1019 , B01J35/1038 , B01J35/1057 , B01J35/1061 , B01J37/0009 , B01J37/0018 , B01J2229/42 , C10G11/05
摘要: The present invention relates to a cracking catalyst composition comprising a physical mixture of 10-90 weight % of a cracking catalyst A and 90-10 weight % of a cracking catalyst B, whereby catalyst A is a zeolite-containing cracking catalyst, and catalyst B is a catalyst having a higher average pore volume in the pore diameter range of 20-200 ANGSTROM than catalyst A in the same pore diameter range and not containing M41S material. These compositions can suitably used for the fluid catalytic cracking of hydrocarbon feeds with high metal concentrations.
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公开(公告)号:EP1363725A2
公开(公告)日:2003-11-26
申请号:EP02718147.8
申请日:2002-02-15
发明人: LAM, Yiu, Lau , DA SILVA SANTOS, Anselmo , RONCOLATTO, Rodolfo, Eugênio , TOREM, Marcelo, André , MORGADO JUNIOR, Edisson , O'CONNOR, Paul
IPC分类号: B01J2/00
CPC分类号: B01J29/088 , B01J35/0006 , B01J35/10 , B01J35/1019 , B01J35/1038 , B01J35/1057 , B01J35/1061 , B01J37/0009 , B01J37/0018 , B01J2229/42 , C10G11/05
摘要: The present invention relates to a cracking catalyst composition comprising a physical mixture of 10-90 weight % of a cracking catalyst A and 90-10 weight % of a cracking catalyst B, whereby catalyst A is a zeolite-containing cracking catalyst, and catalyst B is a catalyst having a higher average pore volume in the pore diameter range of 20-200 Å than catalyst A in the same pore diameter range and not containing M41S material. These compositions can suitably used for the fluid catalytic cracking of hydrocarbon feeds with high metal concentrations.
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