-
公开(公告)号：US20150136646A1
公开(公告)日：2015-05-21
申请号：US14541684
申请日：2014-11-14
IPC分类号： C10M101/02 , C10G67/02
CPC分类号： C10M101/02 , C10G47/06 , C10G65/12 , C10G67/02
摘要： A process is provided for producing a heavy lubricating base oil by hydrocracking a lubricating oil feedstock at high yield. The lubricating oil feedstock contains a hydroprocessed stream that is difficult to process using a conventional catalyst system. The catalyst used in the process includes a mixed metal sulfide catalyst that comprises at least one Group VIB metal and at least one Group VIII metal. The process also provides for hydroisomerization and hydrofinishing process steps to prepare the lubricating base oil.
摘要翻译： 提供了一种通过以高产率加氢裂化润滑油原料来生产重质润滑基础油的方法。 润滑油原料含有使用常规催化剂体系难以加工的加氢处理流。 在该方法中使用的催化剂包括含有至少一种VIB族金属和至少一种第Ⅷ族金属的混合金属硫化物催化剂。 该方法还提供加氢异构化和加氢处理步骤以制备润滑基础油。
-
公开(公告)号：US10196575B2
公开(公告)日：2019-02-05
申请号：US14541684
申请日：2014-11-14
IPC分类号： C10G47/06 , C10G65/12 , C10G67/02 , C10M101/02
摘要： A process is provided for producing a heavy lubricating base oil by hydrocracking a lubricating oil feedstock at high yield. The lubricating oil feedstock contains a hydroprocessed stream that is difficult to process using a conventional catalyst system. The catalyst used in the process includes a mixed metal sulfide catalyst that comprises at least one Group VIB metal and at least one Group VIII metal. The process also provides for hydroisomerization and hydrofinishing process steps to prepare the lubricating base oil.
-
公开(公告)号：US09199224B2
公开(公告)日：2015-12-01
申请号：US14019397
申请日：2013-09-05
IPC分类号： B01J27/051 , B01J27/049 , B01J27/043 , B01J27/047 , B01J35/00 , B01J35/10
CPC分类号： B01J27/0515 , B01J27/043 , B01J27/047 , B01J27/049 , B01J27/051 , B01J35/002 , B01J35/1014 , B01J35/1038 , C10G45/08
摘要： The invention relates to a self-supported mixed metal sulfide (MMS) catalyst for hydrotreating hydrocarbon feedstock and to a method for preparing the catalyst. The MMS catalyst has molar ratios of metal components Ni:Mo:W in a region defined by five points ABCDE of a ternary phase diagram, and wherein the five points ABCDE are defined as: A (Ni=0.72, Mo=0.00, W=0.25), B (Ni=0.25, Mo=0.00, W=0.75), C (Ni=0.25, Mo=0.25, W=0.50), D (Ni=0.60, Mo=0.25, W=0.15), E (Ni=0.72, Mo=0.13, W=0.15).
摘要翻译： 本发明涉及一种用于加氢处理烃原料的自支撑混合金属硫化物（MMS）催化剂及其制备方法。 MMS催化剂在由三元相图的五点ABCDE定义的区域中具有金属成分Ni:Mo:W的摩尔比，其中五点ABCDE定义为：A（Ni = 0.72，Mo = 0.00，W = 0.25），B（Ni = 0.25，Mo = 0.00，W = 0.75），C（Ni = 0.25，Mo = 0.25，W = 0.50），D（Ni = 0.60，Mo = 0.25，W = 0.15） Ni = 0.72，Mo = 0.13，W = 0.15）。
-
公开(公告)号：US20140135207A1
公开(公告)日：2014-05-15
申请号：US14019444
申请日：2013-09-05
IPC分类号： B01J27/051
CPC分类号： B01J27/0515 , B01J27/043 , B01J27/047 , B01J27/049 , B01J27/051 , B01J35/002 , B01J35/1014 , B01J35/1038 , C10G45/08
摘要： The invention relates to a self-supported mixed metal sulfide (MMS) catalyst for hydrotreating hydrocarbon feedstock and to a method for preparing the catalyst. The MMS catalyst is characterized as having a BET surface area of at least 20 m2/g and a pore volume of at least 0.05 cm3/g. In one embodiment, the MMS catalyst is also characterized as having a multi-phased structure comprising five phases: a molybdenum sulfide phase, a tungsten sulfide phase, a molybdenum tungsten sulfide phase, an active nickel phase, and a nickel sulfide phase.
摘要翻译： 本发明涉及一种用于加氢处理烃原料的自支撑混合金属硫化物（MMS）催化剂及其制备方法。 MMS催化剂的特征在于具有至少20m 2 / g的BET表面积和至少0.05cm 3 / g的孔体积。 在一个实施方案中，MMS催化剂的特征还在于具有包含五相的多相结构：硫化钼相，硫化钨相，硫化钨相，活性镍相和硫化镍相。
-
5.发明申请公开(公告)号：US20140066295A1
公开(公告)日：2014-03-06
申请号：US14019379
申请日：2013-09-05
IPC分类号： B01J27/051 , B01J27/049
CPC分类号： B01J27/0515 , B01J27/043 , B01J27/047 , B01J27/049 , B01J27/051 , B01J35/002 , B01J35/1014 , B01J35/1038 , C10G45/08
摘要： A self-supported mixed metal sulfide (MMS) catalyst for hydrotreating hydrocarbon feedstock is disclosed. The self-supported MMS catalyst is characterized by an HDN reaction rate constant of at least 100 g feed hr−1 g catalyst−1 assuming first order kinetics, and an HDS reaction rate constant of at least 550 g feed hr−1 g catalyst−1 assuming first order kinetics in hydrotreating of a Heavy Coker Gas Oil as a feedstock with properties indicated in Table A and at given process conditions as indicated in Table E. In one embodiment, the catalyst is characterized as having a multi-phased structure comprising five phases: a molybdenum sulfide phase, a tungsten sulfide phase, a molybdenum tungsten sulfide phase, an active nickel phase, and a nickel sulfide phase.
摘要翻译： 公开了一种用于加氢处理烃原料的自支撑混合金属硫化物（MMS）催化剂。 自支撑的MMS催化剂的特征在于以假定一级动力学为至少100g进料hr-1g催化剂-1的HDN反应速率常数，以及至少550g进料hr-1g催化剂-1的HDS反应速率常数， 假设在重型Coker Gas Oil作为原料的加氢处理中的一级动力学作为原料，具有表A所示的性质和表E所示的给定工艺条件。在一个实施方案中，催化剂的特征在于具有多相结构，其包含五 相：硫化钼相，硫化钨相，硫化钨相，活性镍相和硫化镍相。
-
公开(公告)号：US20140066296A1
公开(公告)日：2014-03-06
申请号：US14019397
申请日：2013-09-05
IPC分类号： B01J27/051 , B01J27/049
CPC分类号： B01J27/0515 , B01J27/043 , B01J27/047 , B01J27/049 , B01J27/051 , B01J35/002 , B01J35/1014 , B01J35/1038 , C10G45/08
摘要： The invention relates to a self-supported mixed metal sulfide (MMS) catalyst for hydrotreating hydrocarbon feedstock and to a method for preparing the catalyst. The MMS catalyst has molar ratios of metal components Ni:Mo:W in a region defined by five points ABCDE of a ternary phase diagram, and wherein the five points ABCDE are defined as: A (Ni=0.72, Mo=0.00, W=0.25), B (Ni=0.25, Mo=0.00, W=0.75), C (Ni=0.25, Mo=0.25, W=0.50), D (Ni=0.60, Mo=0.25, W=0.15), E (Ni=0.72, Mo=0.13, W=0.15).
摘要翻译： 本发明涉及一种用于加氢处理烃原料的自支撑混合金属硫化物（MMS）催化剂及其制备方法。 MMS催化剂在由三元相图的五点ABCDE定义的区域中具有金属成分Ni:Mo:W的摩尔比，其中五点ABCDE定义为：A（Ni = 0.72，Mo = 0.00，W = 0.25），B（Ni = 0.25，Mo = 0.00，W = 0.75），C（Ni = 0.25，Mo = 0.25，W = 0.50），D（Ni = 0.60，Mo = 0.25，W = 0.15） Ni = 0.72，Mo = 0.13，W = 0.15）。
-
7.发明授权Hydroconversion processes employing multi-metallic catalysts and method for making thereof 有权采用多金属催化剂的加氢转化方法及其制备方法公开(公告)号：US07910761B2
公开(公告)日：2011-03-22
申请号：US12259412
申请日：2008-10-28
CPC分类号： C10G45/08 , B01J23/002 , B01J23/8885 , B01J31/2239 , B01J37/0018 , B01J37/036 , B01J37/20 , B01J2523/00 , B01J2531/26 , B01J2531/66 , B01J2531/847 , C10G45/06 , C10G45/10 , C10G45/12 , C10G45/48 , C10G45/50 , C10G45/52 , C10G45/54 , C10G47/06 , C10G47/18 , C10G47/20 , C10G49/04 , B01J2523/68 , B01J2523/69 , B01J2523/847 , B01J2523/27 , B01J2523/22 , B01J2523/31 , B01J2523/41 , B01J2523/43 , B01J2523/845
摘要： A catalyst precursor composition and methods for making such a catalyst precursor are disclosed. The catalyst precursor comprises at least a promoter metal selected from Group VIII, Group IIB, Group IIA, Group IVA and combinations thereof having an oxidation state of +2 or +4, at least one Group VIB metal having an oxidation state of +6, and at least one organic oxygen-containing ligand. Catalysts prepared from the sulfidation of such catalyst precursors are used in the hydroprocessing of hydrocarbon feeds.
摘要翻译： 公开了催化剂前体组合物和制备这种催化剂前体的方法。 催化剂前体至少包含选自氧化态为+2或+4的VIII族，IIB族，IIA族，IVA族及其组合的至少一种具有+6的氧化态的VIB族金属， 和至少一种有机含氧配体。 由这些催化剂前体的硫化制备的催化剂用于烃进料的加氢处理。
-
公开(公告)号：US09327275B2
公开(公告)日：2016-05-03
申请号：US14019444
申请日：2013-09-05
IPC分类号： B01J27/051 , B01J27/049 , B01J27/043 , B01J27/047 , B01J35/00 , B01J35/10
CPC分类号： B01J27/0515 , B01J27/043 , B01J27/047 , B01J27/049 , B01J27/051 , B01J35/002 , B01J35/1014 , B01J35/1038 , C10G45/08
摘要： The invention relates to a self-supported mixed metal sulfide (MMS) catalyst for hydrotreating hydrocarbon feedstock and to a method for preparing the catalyst. The MMS catalyst is characterized as having a BET surface area of at least 20 m2/g and a pore volume of at least 0.05 cm3/g. In one embodiment, the MMS catalyst is also characterized as having a multi-phased structure comprising five phases: a molybdenum sulfide phase, a tungsten sulfide phase, a molybdenum tungsten sulfide phase, an active nickel phase, and a nickel sulfide phase.
摘要翻译： 本发明涉及一种用于加氢处理烃原料的自支撑混合金属硫化物（MMS）催化剂及其制备方法。 MMS催化剂的特征在于具有至少20m 2 / g的BET表面积和至少0.05cm 3 / g的孔体积。 在一个实施方案中，MMS催化剂的特征还在于具有包含五相的多相结构：硫化钼相，硫化钨相，硫化钨相，活性镍相和硫化镍相。
-
公开(公告)号：US09266098B2
公开(公告)日：2016-02-23
申请号：US14019421
申请日：2013-09-05
IPC分类号： B01J27/051 , B01J27/049 , B01J27/043 , B01J27/047 , B01J35/00 , B01J35/10
CPC分类号： B01J27/0515 , B01J27/043 , B01J27/047 , B01J27/049 , B01J27/051 , B01J35/002 , B01J35/1014 , B01J35/1038 , C10G45/08
摘要： The invention relates to a self-supported mixed metal sulfide (MMS) catalyst for hydrotreating hydrocarbon feedstock and to a method for preparing the catalyst. The MMS catalyst is characterized as having a multi-phased structure comprising five phases: a molybdenum sulfide phase, a tungsten sulfide phase, a molybdenum tungsten sulfide phase, an active nickel phase, and a nickel sulfide phase.
摘要翻译： 本发明涉及一种用于加氢处理烃原料的自支撑混合金属硫化物（MMS）催化剂及其制备方法。 MMS催化剂的特征在于具有包含五相的多相结构：硫化钼相，硫化钨相，硫化钨相，活性镍相和硫化镍相。
-
公开(公告)号：US09205413B2
公开(公告)日：2015-12-08
申请号：US14019457
申请日：2013-09-05
IPC分类号： B01J27/051 , B01J27/049 , B01J27/043 , B01J27/047 , B01J35/00 , B01J35/10
CPC分类号： B01J27/0515 , B01J27/043 , B01J27/047 , B01J27/049 , B01J27/051 , B01J35/002 , B01J35/1014 , B01J35/1038 , C10G45/08
摘要： The invention relates to a method for preparing a self-supported mixed metal sulfide (MMS) catalyst for hydrotreating hydrocarbon feedstock. The method comprises mixing a sufficient amount of a nickel (Ni) metal precursor, a sufficient amount of a molybdenum (Mo) metal precursor, and a sufficient amount of a tungsten (W) metal precursor to produce a catalyst precursor having a molar ratio Ni:Mo:W in relative proportions defined by a region of a ternary phase diagram showing transition metal elemental composition in terms of nickel, molybdenum, and tungsten mol-%, wherein the region is defined by five points ABCDE and wherein the five points are: A (Ni=0.72, Mo=0.00, W=0.28), B (Ni=0.55, Mo=0.00, W=0.45), C (Ni=0.48, Mo=0.14, W=0.38), D (Ni=0.48, Mo=0.20, W=0.33), E (Ni=0.62, Mo=0.14, W=0.24); and sulfiding the catalyst precursor under conditions sufficient to convert the catalyst precursor into a sulfide catalyst.
摘要翻译： 本发明涉及一种用于加氢处理烃原料的自支撑混合金属硫化物（MMS）催化剂的制备方法。 该方法包括混合足量的镍（Ni）金属前体，足够量的钼（Mo）金属前体和足够量的钨（W）金属前体，以制备具有摩尔比Ni ：Mo：相对比例由相对于由镍，钼和钨衍生的过渡金属元素组成的三元相图的区域定义的W，其中该区域由五点ABCDE定义，其中五个点为： A（Ni = 0.72，Mo = 0.00，W = 0.28），B（Ni = 0.55，Mo = 0.00，W = 0.45），C（Ni = 0.48，Mo = 0.14，W = 0.38），D（Ni = 0.48 ，Mo = 0.20，W = 0.33），E（Ni = 0.62，Mo = 0.14，W = 0.24）; 并在足以将催化剂前体转化成硫化物催化剂的条件下硫化催化剂前体。
-
-
-
-
-
-
-
-
-
搜索结果
40 条记录 (耗时 0.103 秒)
