公开(公告)号：US09914113B2

公开(公告)日：2018-03-13

申请号：US13345041

申请日：2012-01-06

申请人： Jeremy Francis ,  Laurent Simon ,  Emmanuelle Guillon ,  Nicolas Bats ,  Avelino Corma ,  Christophe Pichon

发明人： Jeremy Francis ,  Laurent Simon ,  Emmanuelle Guillon ,  Nicolas Bats ,  Avelino Corma ,  Christophe Pichon

IPC分类号： C10G45/12 ,  C10G47/06 ,  C10G65/12 ,  B01J29/04 ,  B01J29/14 ,  B01J29/16 ,  B01J35/00 ,  B01J35/10 ,  B01J37/00 ,  B01J37/02 ,  B01J37/20 ,  C10G49/08

CPC分类号： B01J29/146 ,  B01J29/166 ,  B01J35/002 ,  B01J35/0066 ,  B01J35/109 ,  B01J37/0009 ,  B01J37/0205 ,  B01J37/20 ,  B01J2229/14 ,  B01J2229/16 ,  B01J2229/186 ,  B01J2229/20 ,  B01J2229/36 ,  B01J2229/37 ,  B01J2229/38 ,  B01J2229/42 ,  C10G49/08 ,  C10G2300/301 ,  C10G2300/4018

摘要： Process for hydrocracking and/or hydrotreatment of hydrocarbon feeds utilizing a catalyst comprising at least one hydro-dehydrogenating element of group VIB and of non-precious group VIII used alone or mixed, and a support comprising at least one porous mineral matrix and at least one dealuminated USY zeolite having an overall silicon-to-aluminium atomic ratio comprised between 2.5 and 10, a fraction by weight of extra-network aluminium atom greater than 10% relative to the total mass of the aluminium present in the zeolite, a mesopore volume measured by nitrogen porosimetry greater than 0.07 ml.g−1, and a crystal parameter a0 of the elemental mesh greater than 24.28 Å, in which a quantity of the element nickel comprised between 0.5 and 3% by weight relative to the total mass of the zeolite is deposited on said USY zeolite and in which said catalyst is in the sulphide form.

公开(公告)号：US20120205286A1

公开(公告)日：2012-08-16

申请号：US13345041

申请日：2012-01-06

申请人： Jeremy FRANCIS ,  Laurent Simon ,  Emmanuelle Guillon ,  Nicolas Bats ,  Avelino Corma ,  Christophe Pichon

发明人： Jeremy FRANCIS ,  Laurent Simon ,  Emmanuelle Guillon ,  Nicolas Bats ,  Avelino Corma ,  Christophe Pichon

IPC分类号： C10G65/12 ,  B01J29/04 ,  C10G47/06

CPC分类号： B01J29/146 ,  B01J29/166 ,  B01J35/002 ,  B01J35/0066 ,  B01J35/109 ,  B01J37/0009 ,  B01J37/0205 ,  B01J37/20 ,  B01J2229/14 ,  B01J2229/16 ,  B01J2229/186 ,  B01J2229/20 ,  B01J2229/36 ,  B01J2229/37 ,  B01J2229/38 ,  B01J2229/42 ,  C10G49/08 ,  C10G2300/301 ,  C10G2300/4018

摘要： Process for hydrocracking and/or hydrotreatment of hydrocarbon feeds utilizing a catalyst comprising at least one hydro-dehydrogenating element of group VIB and of non-precious group VIII used alone or mixed, and a support comprising at least one porous mineral matrix and at least one dealuminated USY zeolite having an overall silicon-to-aluminium atomic ratio comprised between 2.5 and 10, a fraction by weight of extra-network aluminium atom greater than 10% relative to the total mass of the aluminium present in the zeolite, a mesopore volume measured by nitrogen porosimetry greater than 0.07 ml.g−1, and a crystal parameter a0 of the elemental mesh greater than 24.28 Å, in which a quantity of the element nickel comprised between 0.5 and 3% by weight relative to the total mass of the zeolite is deposited on said USY zeolite and in which said catalyst is in the sulphide form.

摘要翻译： 使用包含至少一种单独或混合使用的VIB族和非贵重族VIII的加氢脱氢元素的催化剂，以及包含至少一种多孔矿物基质和至少一种多孔矿物基质的载体来加氢裂化和/或加氢处理烃进料的方法 具有2.5至10的整体硅 - 铝原子比的脱铝USY沸石，相对于存在于沸石中的铝的总质量大于10％的网络外铝原子的重量百分比，测量的中孔体积 通过氮气孔隙度法大于0.07ml.g-1，并且元素网的晶体参数a0大于24.28，其中元素镍的量相对于沸石的总质量为0.5-3重量％ 沉积在所述USY沸石上，其中所述催化剂为硫化物形式。