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公开(公告)号：US09035115B2
公开(公告)日：2015-05-19
申请号：US13315650
申请日：2011-12-09
CPC分类号： C10G45/62 , B01J23/8885 , B01J37/20 , C10G3/42 , C10G3/46 , C10G3/50 , C10G45/60 , C10G2300/1014 , C10G2300/1055 , C10G2300/1088 , Y02E50/14 , Y02P30/20
摘要： A hydrocarbon conversion process comprises contacting a renewable feedstock under hydroprocessing conditions with a bulk catalyst to form oleochemicals such as fatty alcohols, esters, and normal paraffins. Advantageously, the reaction conditions can be selected to directly convert the renewable feedstock to the desired product(s).
摘要翻译： 烃转化方法包括在加氢处理条件下将可再生原料与本体催化剂接触以形成油脂化学物质，例如脂肪醇，酯和正链烷烃。 有利地，可以选择反应条件以将可再生原料直接转化为所需的产物。
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公开(公告)号：US08884077B2
公开(公告)日：2014-11-11
申请号：US13315575
申请日：2011-12-09
IPC分类号： C07C29/149
CPC分类号： C11B3/02
摘要： A hydrocarbon conversion process comprises contacting a renewable feedstock under hydroprocessing conditions with a bulk catalyst to form oleochemicals such as fatty alcohols, esters, and normal paraffins. Advantageously, the reaction conditions can be selected to directly convert the renewable feedstock to the desired product(s).
摘要翻译： 烃转化方法包括在加氢处理条件下将可再生原料与本体催化剂接触以形成油脂化学物质，例如脂肪醇，酯和正链烷烃。 有利地，可以选择反应条件以将可再生原料直接转化为所需的产物。
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公开(公告)号：US08704007B2
公开(公告)日：2014-04-22
申请号：US13315611
申请日：2011-12-09
IPC分类号： C07C27/04
CPC分类号： C07C29/149 , C07C29/177 , C07C67/00 , C10G3/46 , C10G3/50 , C10G2300/1014 , C10G2300/1018 , Y02P30/20 , C07C31/125 , C07C69/26
摘要： A hydrocarbon conversion process comprises contacting a renewable feedstock under hydroprocessing conditions with a bulk catalyst to form oleochemicals such as fatty alcohols, esters, and normal paraffins. Advantageously, the reaction conditions can be selected to directly convert the renewable feedstock to the desired product(s).
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公开(公告)号：US20130150631A1
公开(公告)日：2013-06-13
申请号：US13315611
申请日：2011-12-09
IPC分类号： C07C29/00
CPC分类号： C07C29/149 , C07C29/177 , C07C67/00 , C10G3/46 , C10G3/50 , C10G2300/1014 , C10G2300/1018 , Y02P30/20 , C07C31/125 , C07C69/26
摘要： A hydrocarbon conversion process comprises contacting a renewable feedstock under hydroprocessing conditions with a bulk catalyst to form oleochemicals such as fatty alcohols, esters, and normal paraffins. Advantageously, the reaction conditions can be selected to directly convert the renewable feedstock to the desired product(s).
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公开(公告)号：US20130150600A1
公开(公告)日：2013-06-13
申请号：US13315575
申请日：2011-12-09
IPC分类号： C11B3/02
CPC分类号： C11B3/02
摘要： A hydrocarbon conversion process comprises contacting a renewable feedstock under hydroprocessing conditions with a bulk catalyst to form oleochemicals such as fatty alcohols, esters, and normal paraffins. Advantageously, the reaction conditions can be selected to directly convert the renewable feedstock to the desired product(s).
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公开(公告)号：US20140163249A1
公开(公告)日：2014-06-12
申请号：US13708811
申请日：2012-12-07
申请人： Cong-Yan Chen , Alexander E. Kuperman , William James Cannella , Theodorus Ludovicus Michaael Maesen
发明人： Cong-Yan Chen , Alexander E. Kuperman , William James Cannella , Theodorus Ludovicus Michaael Maesen
IPC分类号： C07C29/149 , C11C3/12 , C10G3/00
CPC分类号： C07C29/149 , C10G3/46 , C10G3/50 , C10G45/58 , C10G50/02 , C10G69/14 , C10G2300/1022 , C10G2400/10 , C11C3/00 , C11C3/123 , Y02P30/20 , C07C31/125
摘要： A hydroconversion process comprises contacting a feedstock comprising renewable materials under hydroprocessing conditions with a promoted catalyst selected from a self-supported catalyst, a supported catalyst and combinations thereof, wherein the reaction conditions can be tailored to directly convert the renewable feedstock to the desired product(s) including fatty alcohols, esters, normal paraffins, or combinations thereof. The catalyst comprising at least a Group VIB metal selected from molybdenum and tungsten, a Group VIII metal selected from cobalt and nickel to convert the feedstock into any of fatty alcohols, esters, and normal paraffins. In some embodiments, the process further comprising additional steps to generate various desirable products, including α-olefins (or PAO, by dehydrating the fatty alcohol products), lubricants and bright stocks (from the oligomerizing of the PAO), and Group 3 lubricants (from co-oligomerizing of the PAO with some short chain olefins).
摘要翻译： 加氢转化方法包括在加氢处理条件下将包含可再生材料的原料与选自自支撑催化剂，负载型催化剂及其组合的促进催化剂接触，其中反应条件可以被定制以将可再生原料直接转化为所需产物（ s），包括脂肪醇，酯，正链烷烃或其组合。 所述催化剂至少包含选自钼和钨的第VIB族金属，选自钴和镍的第Ⅷ族金属，以将原料转化成任何脂肪醇，酯和正链烷烃。 在一些实施方案中，该方法还包括产生各种所需产物的其它步骤，包括α-烯烃（或PAO，通过脱脂脂肪醇产物），润滑剂和光亮油料（来自PAO的低聚）和第3组润滑剂 来自PAO与一些短链烯烃的共低聚）。
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公开(公告)号：US20090107880A1
公开(公告)日：2009-04-30
申请号：US11932751
申请日：2007-10-31
摘要： A process of upgrading a heavy hydrocarbon feedstock comprising contacting a heavy hydrocarbon feedstock with a catalyst in the presence of hydrogen in a reactor system, containing the catalyst as the only catalyst, wherein the catalyst, is prepared by sulfiding a catalyst precursor obtained by mixing at reaction conditions, to form a precipitate or cogel, at least a Group VIII metal compound in solution; at least a Group VIB metal compound in solution; and, at least an organic oxygen containing ligand in solution, and thereby producing a fuel product.
摘要翻译： 一种升级重质烃原料的方法，包括在氢气存在下使重烃原料与催化剂在反应器系统中接触，反应器系统含有催化剂作为唯一的催化剂，其中催化剂是通过将通过混合获得的催化剂前体硫化 在溶液中形成沉淀物或共凝胶，至少第VIII族金属化合物; 溶液中至少含有VIB族金属化合物; 和在溶液中至少含有机氧的配体，从而生产燃料产物。
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公开(公告)号：US20090114566A1
公开(公告)日：2009-05-07
申请号：US12260877
申请日：2008-10-29
IPC分类号： C10G47/02
CPC分类号： C10G49/002 , C10G45/04 , C10G45/46 , C10G45/60 , C10G49/02 , C10G2400/08
摘要： A process of upgrading a heavy hydrocarbon feedstock comprising contacting a heavy hydrocarbon feedstock with a catalyst in the presence of hydrogen in a reactor system, containing the catalyst as the only catalyst, wherein the catalyst, is prepared by sulfiding a catalyst precursor obtained by mixing at reaction conditions, to form a precipitate or cogel, at least a Promoter metal compound in solution; at least a Group VIB metal compound in solution; and, at least an organic oxygen containing ligand in solution, and thereby producing a fuel product.
摘要翻译： 一种升级重质烃原料的方法，包括在氢气存在下使重烃原料与催化剂在反应器系统中接触，反应器系统含有催化剂作为唯一的催化剂，其中催化剂是通过将通过混合获得的催化剂前体硫化 反应条件，以形成沉淀或共凝胶，至少在溶液中的促进剂金属化合物; 溶液中至少含有VIB族金属化合物; 和在溶液中至少含有机氧的配体，从而生产燃料产物。
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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。
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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。
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