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公开(公告)号:EP1169416A4
公开(公告)日:2003-03-26
申请号:EP00908284
申请日:2000-01-14
IPC分类号: C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00
CPC分类号: 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
摘要: Hydroprocessing of petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
摘要翻译: 使用批量VIII族/ VIB族催化剂石油化工原料的加氢处理。 优选的催化剂包括那些含有镍 - 钼 - W的。
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2.HYDROCRACKING PROCESS USING BULK GROUP VIII/GROUP VIB CATALYSTS 有权
标题翻译: VERFAHREN ZUR HYDROCRACKUNG MIT KATALYSATOREN DER GRUPPEN VIII UND VIB INSCHÜTTGUTFORM公开(公告)号:EP1157083A4
公开(公告)日:2003-03-26
申请号:EP00909912
申请日:2000-01-14
发明人: SOLED STUART LEON , RILEY KENNETH LLOYD , SCHLEICHER GARY P , DEMMIN RICHARD A , SCHUETTE WILLIAM LEE , CODY IAN ALFRED
IPC分类号: C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00
CPC分类号: 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
摘要: Hydrocracking process for hydrocracking petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
摘要翻译: 使用批量第VIII / VIB族催化剂对石油和化学原料进行加氢处理。 优选的催化剂包括由Ni-Mo-W组成的催化剂。
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3.HYDROFINING PROCESS USING BULK GROUP VIII/GROUP VIB CATALYSTS 有权
标题翻译: 使用组VIII / VIb的散装形式催化剂的方法HYDRORAFFINERIERUNG公开(公告)号:EP1171549A4
公开(公告)日:2003-01-02
申请号:EP00908287
申请日:2000-01-14
IPC分类号: C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00
CPC分类号: 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
摘要: Hydroprocessing of petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
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公开(公告)号:EP1054939A4
公开(公告)日:2005-02-09
申请号:EP99906943
申请日:1999-02-12
发明人: RILEY KENNETH LLOYD , MURPHY WILLIAM JOHN , CODY IAN ALFRED , SOLED STUART LEON , MCVICKER GARY BRICE , MISEO SABATO
IPC分类号: C07C5/00 , C07C5/13 , C07C5/22 , C10G21/00 , C10G35/04 , C10G35/06 , C10G35/095 , C10G45/62 , C10G45/64 , C10G67/04 , C10G71/00 , C10G45/60
CPC分类号: C10G45/64 , C10G45/62 , C10G2400/10
摘要: 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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5.TWO STAGE PROCESS FOR HYDRODESULFURIZING DISTILLATES USING BULK MULTIMETALLIC CATALYST 有权
标题翻译: 两阶段的过程FOR DISTILLATENMIT帮助更多的金属催化剂加氢脱硫散装形式公开(公告)号:EP1169414A4
公开(公告)日:2003-01-29
申请号:EP00905623
申请日:2000-01-14
发明人: RILEY KENNETH LLOYD , KLEIN DARRYL PATRICK , HOU ZHIGUO , SOLED STUART LEON , KERBY MICHAEL CHARLES , MCVICKER GARY BRICE , ELLIS EDWARD STANLEY , TOUVELLE MICHELE SUE , MISEO SABATO
IPC分类号: C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00 , C10G45/04 , C10G29/04
CPC分类号: 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
摘要: A two stage hydrodesulfurizing process for producing low sulfur distillates. A distillate boiling range feedstock containing in excess of about 3,000 wppm sulfur is hydrodesulfurized in a first hydrodesulfurizing stage containing one or more reaction zones in the presence of hydrogen and a hydrodesulfurizing catalyst. The liquid product stream thereof is passed to a first separation stage wherein a vapor phase product stream and a liquid product stream are produced. The liquid product stream, which has a substantially lower sulfur and nitrogen content than the original feedstream is passed to a second hydrodesulfurizing stage also containing one or more reaction zones where it is reacted in the presence of hydrogen and a second hydrodesulfurizing catalyst at hydrodesulfurizing conditions. The catalyst in any one or more reaction zones is a bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least two Group VIB metals.
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6.HYDROTREATING OR RAW VIRGIN DISTILLATES USING NOVEL BULK MULTIMETALLIC CATALYSTS 审中-公开
标题翻译: HYDRIERUNG VON ROHDESTILLATEN MIT NEUEM MEHRMETALLISCHEM KATALYSATOR INSCHÜTTGUTFORM公开(公告)号:EP1169411A4
公开(公告)日:2003-01-08
申请号:EP00908283
申请日:2000-01-14
发明人: RILEY KENNETH LLOYD , KLEIN DARRYL PATRICK , HOU ZHIGUO , SOLED STUART LEON , KERBY MICHAEL CHARLES , MCVICKER GARY BRICE , ELLIS EDWARD STANLEY , TOUVELLE MICHELE SUE , MISEO SABATO
IPC分类号: C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00
CPC分类号: 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
摘要: Hydroprocessing of petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
摘要翻译: 使用批量第VIII / VIB族催化剂对石油和化学原料进行加氢处理。 优选的催化剂包括由Ni-Mo-W组成的催化剂。
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公开(公告)号:EP1169417A4
公开(公告)日:2003-03-26
申请号:EP00908286
申请日:2000-01-14
IPC分类号: C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00 , C10G71/00
CPC分类号: 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
摘要: Hydroprocessing of petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
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8.HYDROCONVERSION PROCESS USING BULK GROUP VIII/GROUP VIB CATALYSTS 有权
标题翻译: 方法HYDRO转换使用组和八VIB的催化剂散装形式公开(公告)号:EP1171547A4
公开(公告)日:2003-01-29
申请号:EP00908288
申请日:2000-01-14
IPC分类号: C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00
CPC分类号: 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
摘要: Hydroconversion processing of 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.MULTISTAGE PROCESS FOR HYDRODESULFURIZING-HYDROGENATING DISTILLATES USING BULK MULTIMETALLIC CATALYST 审中-公开
标题翻译: 多阶段过程FOR DISTILLATEN的HYDRODESULPHORIERUNG加氢与散装形式更多金属催化剂公开(公告)号:EP1169413A4
公开(公告)日:2003-01-29
申请号:EP00904363
申请日:2000-01-14
发明人: RILEY KENNETH LLOYD , KLEIN DARRYL PATRICK , HOU ZHIGUO , SOLED STUART LEON , KERBY MICHAEL CHARLES , MCVICKER GARY BRICE , ELLIS EDWARD STANLEY , TOUVELLE MICHELE SUE , MISEO SABATO
IPC分类号: C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00 , C10G45/04 , B01J23/30 , C10G29/04
CPC分类号: 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
摘要: A two stage hydrodesulfurizing process for producing low sulfur distillates. A distillate boiling range feedstock containing in excess of about 3,000 wppm sulfur is hydrodesulfurized in a first hydrdesulfurzing stage containing one or more reaction ones in the presence of hydrogen and a hydrodesulfurizing catalyst. The liquid product stream thereof is passed to a first separation stage wherein a vapor phase product stream and a liquid product stream are produced. The liquid product stream, which has a substantially lower sulfur and nitrogen content than the original feedstream is passed to a second hydrodesulfurizing stage also containing one or more reaction zones where it is reacted in the presence of hydrogen and a second hydrodesulfurizing catalyst at hydrodesulfurizing conditions. The catalyst in any one or more reaction zones is a bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least two Group VIB metals.
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10.HYDROPROCESSING USING BULK GROUP VIII/GROUP VIB CATALYSTS 审中-公开
标题翻译: VERFAHREN ZUR HYDROCRACKUNG MIT KATALYSATOREN DER GRUPPEN VIII UND VIB公开(公告)号:EP1169415A4
公开(公告)日:2003-01-08
申请号:EP00905627
申请日:2000-01-14
发明人: SOLED STUART LEON , MISEO SABATO , KRYCAK ROMAN , VROMAN HILDA B , HO TEH CHUNG , RILEY KENNETH LLOYD
IPC分类号: C01G53/00 , B01J23/00 , B01J23/85 , B01J23/86 , B01J23/88 , B01J23/883 , B01J23/888 , B01J27/049 , B01J27/051 , B01J27/24 , B01J37/03 , B01J37/08 , B01J37/20 , C07B61/00 , C07C29/16 , C07C31/125 , C08F8/00 , C08F8/04 , C08F8/50 , C10C1/18 , C10C3/00 , C10C3/04 , C10C3/08 , C10G11/00 , C10G11/02 , C10G11/04 , C10G21/16 , C10G21/20 , C10G45/08 , C10G45/16 , C10G45/38 , C10G45/50 , C10G45/60 , C10G45/64 , C10G47/02 , C10G47/04 , C10G47/12 , C10G47/24 , C10G49/04 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G65/16 , C10G67/02 , C10G67/04 , C10G67/14 , C10G69/02 , C10M101/02 , C10M177/00 , C10N20/00 , C10N20/02 , C10N70/00
CPC分类号: 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
摘要: Hydroprocessing of petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni-Mo-W.
摘要翻译: 使用批量第VIII / VIB族催化剂对石油和化学原料进行加氢处理。 优选的催化剂包括由Ni-Mo-W组成的催化剂。
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