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1.发明公开
公开(公告)号：EP1578712A2
公开(公告)日：2005-09-28
申请号：EP03779969.9
申请日：2003-11-18
Inventor： SOLED, Stuart, Leon , MALEK, Andrzej , VARTULI, James, Clarke , FEELEY, Jennifer, Schaefer , MISEO, Sabato , LUO, Shifang , SCHLOSBERG, Richard Henry , BAUMGARTNER, Joseph, Ernest , KLIEWER, Christine, E. , RAGOMO, Steven, T.
IPC: C07C51/00
CPC classification number: C08F8/04 , B01J23/462 , B01J23/75 , B01J35/0053 , B01J35/0066 , B01J35/1023 , B01J35/1028 , B01J35/1061 , B01J37/0203 , B01J37/08 , B01J37/082 , C07C29/19 , C07C67/303 , C07C69/75
Abstract: The present invention is directed to a process for hydrogenating one or more organic compounds especially unsaturated organic compounds by bringing the compound into contact with a hydrogen-containing gas in the presence of a catalyst, which comprises one or more catalytically active metals applied to a porous catalyst support. The one or more catalytically active metals having been derived via a decomposed organic complex of the metal on the support, in particular amine complexes of the metal. The decomposed complex may be treated with hydrogen to activate the catalyst before use as a hydrogenation catalyst.
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公开(公告)号：EP2831205A1
公开(公告)日：2015-02-04
申请号：EP13717370.4
申请日：2013-03-28
Applicant: ExxonMobil Research and Engineering Company
Inventor： FINGLAND, Bradley, R. , HANKS, Patrick, Loring , SOLED, Stuart, Leon , MISEO, Sabato
IPC: C10G45/04 , B01J21/10 , B01J23/06 , B01J23/28 , B01J23/30 , C10G65/04 , C10G3/00 , B01J23/00 , B01J23/888
CPC classification number: C10G3/47 , B01J23/002 , B01J23/882 , B01J23/883 , B01J23/888 , B01J23/8885 , B01J35/1014 , B01J35/1019 , B01J37/20 , B01J2523/00 , C10G3/46 , C10G45/04 , C10G65/04 , C10G2300/202 , Y02P30/20 , B01J2523/68 , B01J2523/69 , B01J2523/847
Abstract: This invention relates to methods for deoxygenation utilizing bulk metal catalysts feedstocks derived in part or whole from biological sources and alternatively, further hydrotreatment processing of such deoxygenated feedstocks. Feedstocks containing bio-derived feed components, and preferably additionally mineral oil feed components, are deoxygenated in a first stage or zone using a bulk metal catalyst. In additional embodiments, the deoxygenated feedstock effluent from the deoxygenation stage is further subjected to a hydrodesulfurization stage or zone.
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公开(公告)号：EP1446226A2
公开(公告)日：2004-08-18
申请号：EP02803155.7
申请日：2002-10-15
Applicant: ExxonMobil Research and Engineering Company
Inventor： SOLED, Stuart, Leon , BAUMGARTNER, Joseph, Ernest , KISS, Gabor
IPC: B01J38/00
CPC classification number: C10G2/332 , B01J23/94 , B01J23/96 , B01J38/10 , B01J38/12 , C10G2/00 , C10G2/333
Abstract: An in situ process for conducting regeneration of spent hydrocarbon synthesis catalyst. Regenerated, but not yet re-activated, catalyst (15) may be introduced into an operating HCS reactor (1) that has catalyst rejuvenation means (14). Any combination of a fresh, activated catalyst, a fresh, passivated catalyst or short-term or long-term deactivated catalysts may already be present in the HCS reactor (1). The regenerated, but not yet re-activated catalyst is activated in the HCS reactor (1) with rejuvenation means (14) at normal process conditions. The HCS reactor (1) receives syngas through the inlet line (3) and releases liquid hydrocarbons through outlet line (4) and gaseous hydrocarbon and unreacted syngas through the offgas line (2). Catalyst is removed from the HCS reactor (1) through the slipstream line (5) and into a filtration unit (6) which is fed with a stripping fluid (7). The filtered catalyst proceeds to the regeneration unit (9) which is fed a regenerative fluid (10). The regenerated catalyst is returned to the HCS Reactor (1) through the catalyst return line (11) where it is reactivated.
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公开(公告)号：EP1169415A1
公开(公告)日：2002-01-09
申请号：EP00905627.6
申请日：2000-01-14
Applicant: ExxonMobil Research and Engineering Company
Inventor： SOLED, Stuart, Leon , MISEO, Sabato , KRYCAK, Roman , VROMAN, Hilda, B. , HO, Teh, Chung , RILEY, Kenneth, Lloyd
CPC classification number: B01J23/002 , B01J23/85 , B01J23/88 , B01J23/883 , B01J23/8878 , B01J23/888 , B01J23/8885 , B01J37/03 , B01J37/082 , B01J2523/00 , C08F8/00 , C08F8/04 , C08F8/50 , C10G45/08 , C10G45/16 , C10G47/04 , C10G65/04 , C10G65/08 , C10G65/12 , C10G2300/1062 , C10G2300/301 , C10G2300/302 , C10G2300/4018 , C10G2300/44 , C10G2400/10 , C10G2400/14 , C08F240/00 , B01J2523/68 , B01J2523/69 , B01J2523/842 , B01J2523/67 , B01J2523/847 , B01J2523/31 , B01J2523/41
Abstract: A process fo hydroprocessing petroleum and chemical feedstocks by use of a bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least one, preferably two Group VIB metal wherein the ratio of Group VIB metal to Group VIII metal is from about 10:1 to 1:10.
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公开(公告)号：EP1062296A1
公开(公告)日：2000-12-27
申请号：EP98963928.1
申请日：1998-12-15
Applicant: ExxonMobil Research and Engineering Company
Inventor： GORBATY, Martin, Leo , FERRUGHELLI, David, Thomas , OLMSTEAD, William, Neergaard , MISEO, Sabato , SOLED, Stuart, Leon , ROBBINS, Winston, Karl
CPC classification number: C10G25/003 , C10G25/00
Abstract: The present invention is a process to remove a major portion of metals and coke precursors from a hydrocarbon stream. The steps of the process include contacting the feedstream with a hydrocarbon insoluble adsorbent, recovering the oil which does not adsorb and removing the metals and coke precursors from the adsorbent.
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Patent Agency Ranking
公开(公告)号：EP1737930A1
公开(公告)日：2007-01-03
申请号：EP05736489.5
申请日：2005-04-19
Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY
Inventor： SOLED, Stuart, Leon , MISEO, Sabato , EIJSBOUTS, Sonja
IPC: C10G45/08 , B01J23/887 , B01J27/051 , B01J27/049 , B01J23/888
CPC classification number: C10G45/08 , B01J23/8877 , B01J23/888 , B01J37/0009 , B01J37/04 , C10G65/02
Abstract: The instant invention relates to a process to produce low sulfur distillate products through the hydrotreating of distillate boiling range feedstreams in the presence of a bulk metal hydrotreating catalyst, which comprises: i) a Group VIB metal component selected from molybdenum, tungsten and mixtures thereof; ii) a Group V metal component selected from vanadium, niobium, tantalum, and mixtures thereof; and iii) a Group VIII metal component selected from nickel, cobalt, iron, and mixtures thereof, wherein the metal components, calculated as oxides, comprise at least 50 wt.% of the catalyst based on the weight of the catalysts, and wherein the molar ratio between the metal components, expressed by the formula (Group VIB + Group V) : (Group VIII), ranges from 0.35:1 to 2:1.
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公开(公告)号：EP1169416B1
公开(公告)日：2005-08-24
申请号：EP00908284.3
申请日：2000-01-14
Applicant: ExxonMobil Research and Engineering Company
Inventor： RILEY, Kenneth, Lloyd , SCHUETTE, William, Lee , SOLED, Stuart, Leon , MISEO, Sabato
CPC classification number: B01J23/002 , B01J23/85 , B01J23/88 , B01J23/883 , B01J23/8878 , B01J23/888 , B01J23/8885 , B01J37/03 , B01J37/082 , B01J2523/00 , C08F8/00 , C08F8/04 , C08F8/50 , C10G45/08 , C10G45/16 , C10G47/04 , C10G65/04 , C10G65/08 , C10G65/12 , C10G2300/1062 , C10G2300/301 , C10G2300/302 , C10G2300/4018 , C10G2300/44 , C10G2400/10 , C10G2400/14 , C08F240/00 , B01J2523/68 , B01J2523/69 , B01J2523/842 , B01J2523/67 , B01J2523/847 , B01J2523/31 , B01J2523/41
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8.发明公开
公开(公告)号：EP1157083A1
公开(公告)日：2001-11-28
申请号：EP00909912.8
申请日：2000-01-14
Applicant: ExxonMobil Research and Engineering Company
Inventor： SOLED, Stuart, Leon , RILEY, Kenneth, Lloyd , SCHLEICHER, Gary, P. , DEMMIN, Richard, A. , SCHUETTE, William, Lee , CODY, Ian, Alfred
CPC classification number: B01J23/002 , B01J23/85 , B01J23/88 , B01J23/883 , B01J23/8878 , B01J23/888 , B01J23/8885 , B01J37/03 , B01J37/082 , B01J2523/00 , C08F8/00 , C08F8/04 , C08F8/50 , C10G45/08 , C10G45/16 , C10G47/04 , C10G65/04 , C10G65/08 , C10G65/12 , C10G2300/1062 , C10G2300/301 , C10G2300/302 , C10G2300/4018 , C10G2300/44 , C10G2400/10 , C10G2400/14 , C08F240/00 , B01J2523/68 , B01J2523/69 , B01J2523/842 , B01J2523/67 , B01J2523/847 , B01J2523/31 , B01J2523/41
Abstract: Hydrocracking process for hydrocracking petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
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9.发明公开SLURRY HYDROPROCESSING USING BULK MULTIMETALLIC CATALYSTS 有权悬挂BRENNSTROFFEN加氢散体形，Mehere METALS综合催化剂
公开(公告)号：EP1153106A1
公开(公告)日：2001-11-14
申请号：EP00904366.2
申请日：2000-01-14
Applicant: Exxonmobil Research and Engineering Company
Inventor： HOU, Zhiguo , BEARDEN, Roby, Jr. , FERRUGHELLI, David, Thomas , MISEO, Sabato , GORBATY, Martin, Leo , SOLED, Stuart, Leon
CPC classification number: B01J23/002 , B01J23/85 , B01J23/88 , B01J23/883 , B01J23/8878 , B01J23/888 , B01J23/8885 , B01J37/03 , B01J37/082 , B01J2523/00 , C08F8/00 , C08F8/04 , C08F8/50 , C10G45/08 , C10G45/16 , C10G47/04 , C10G65/04 , C10G65/08 , C10G65/12 , C10G2300/1062 , C10G2300/301 , C10G2300/302 , C10G2300/4018 , C10G2300/44 , C10G2400/10 , C10G2400/14 , C08F240/00 , B01J2523/68 , B01J2523/69 , B01J2523/842 , B01J2523/67 , B01J2523/847 , B01J2523/31 , B01J2523/41
Abstract: A slurry hydroprocessing process for upgrading a hydrocarbon feedstock containing nitrogen and sulfur using bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least two Group VIB metals wherein the ratio of Group VIB metal to Group VIII metal is about 10:1 to about 1:10.
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公开(公告)号：EP1054939A1
公开(公告)日：2000-11-29
申请号：EP99906943.8
申请日：1999-02-12
Applicant: ExxonMobil Research and Engineering Company
Inventor： RILEY, Kenneth, Lloyd , MURPHY, William, John , CODY, Ian, Alfred , SOLED, Stuart, Leon , McVICKER, Gary, Brice , MISEO, Sabato
CPC classification number: C10G45/64 , C10G45/62 , C10G2400/10
Abstract: Waxy feeds are treated under hydroisomerization conditions to produce good yields of an isomerate product of high VI by using a silica-alumina based catalyst in which the silica-alumina has a pore volume less of 0.99 ml/gm (H2O), an alumina content in the range of 35 to 55 wt.% and an isoelectric point in the range of 4.5 to 6.5. A lube fraction of the isomerate is dewaxed to provide a lube basestock of high VI. The silica-alumina may be modified with a rare earth oxide or yttria or boria or magnesia in which instance the modified catalyst has an isoelectric point greater than but no more than 2 points greater than the base silica alumina.
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