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1.
公开(公告)号:EP0641299A4
公开(公告)日:1994-12-16
申请号:EP93912292
申请日:1993-04-19
申请人: MOBIL OIL CORP
CPC分类号: B01J29/7042 , B01J29/65 , B01J29/7046 , B01J2229/26 , B01J2229/37 , B01J2229/42 , C07C5/2775 , C07C11/02
摘要: In a process for skeletal isomerization of linear olefins to iso-olefins, e.g., n-butenes to isobutylene, over a catalyst comprising medium pore zeolite, e.g., a zeolite selected from ZSM-22, ZSM-23, and ZSM-35, the zeolite is pretreated with a dicarboxylic acid, e.g., oxalic acid. The pretreatment significantly reduces aging rate and increases cycle length of the catalyst.
摘要翻译: 在包含中孔沸石(例如选自ZSM-22,ZSM-23和ZSM-35的沸石)的催化剂上,直链烯烃骨架异构化为异烯烃例如正丁烯异丁烯的方法中, 沸石用二羧酸例如草酸预处理。 预处理显着降低了老化速率并增加了催化剂的循环长度。
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公开(公告)号:EP0553562B1
公开(公告)日:1997-12-29
申请号:EP92311632
申请日:1992-12-21
申请人: MOBIL OIL CORP
CPC分类号: B01J29/7007 , B01J2229/16 , Y10S423/27
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公开(公告)号:EP0596022A4
公开(公告)日:1994-08-17
申请号:EP92917029
申请日:1992-07-23
申请人: MOBIL OIL CORP
发明人: APELIAN MINAS ROBERT , DEGNAN THOMAS FRANCIS JR , MARLER DAVID OWEN , MAZZONE DOMINICK NICHOLAS
CPC分类号: C10G47/16 , B01J29/042 , B01J29/044 , B01J29/045 , B01J2229/42
摘要: A process for producing high quality lubricants by hydrocracking a high boiling hydrocarbon feed in the presence of hydrogen and a bifunctional hydrocracking catalyst based on an ultra-large pore crystalline material. The crystalline material exhibits unusually large pores of at least 13 Å diameter and a high sorption capacity demonstrated by its benzene adsorption capacity of greater than 15 grams benzene/100 grams at 6.7 kPa (50 Torr) and 25 °C. The crystalline material is characterized by an X-ray diffraction pattern with at least one d-spacing greater than 18 Å and in a particularly preferred form, a hexagonal arrangement of pores of at least 13 Å diameter which can be indexed with a d100 value greater than 18 Å. The hydrocracking catalysts based on these materials are capable of producing hydrocracked lube products of good viscosity index in high yields without the use of fluorine or other promoters. Petroleum waxes may be used as the feed and is hydrocracked and hydroisomerized to form the lube products.
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公开(公告)号:EP0788533A4
公开(公告)日:1998-08-05
申请号:EP95935723
申请日:1995-10-13
申请人: MOBIL OIL CORP
CPC分类号: C10G73/00 , C10G2400/10
摘要: This invention discloses a process for producing a high Viscosity Index lubricant having a viscosity of at least 125 from a waxy hydrocarbon feed having a wax content of at least 40 wt.%. The process comprises catalytically dewaxing waxy paraffins present in the feed primarily by isomerization, in the presence of hydrogen and in the presence of a low acidity large pore zeolite molecular sieve having a crystal size of less than 0.1 micron, an alpha value of not more than 30 and containing a noble metal hydrogenation component. The large pore zeolite is preferably zeolite beta loaded with 0.3 to 2 wt.% Pt. The feed may be hydrocracked prior to dewaxing with the large pore zeolite. The effluent of the process may also be further dewaxed by either solvent or catalytic means in order to achieve target pour point.
摘要翻译: 本发明公开了由蜡含量至少为40重量%的含蜡烃进料生产粘度至少为125的高粘度指数润滑剂的方法。 该方法包括主要通过异构化在存在氢气的情况下并且在具有小于0.1微米的晶体尺寸的低酸度大孔沸石分子筛的存在下催化脱蜡进料中存在的蜡状链烷烃,α值不超过 30并含有贵金属氢化组分。 大孔沸石优选负载有0.3至2重量%Pt的沸石β。 进料可以在用大孔沸石脱蜡之前进行加氢裂化。 该方法的流出物也可以通过溶剂或催化剂进一步脱蜡以达到目标倾点。
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公开(公告)号:EP0641375B1
公开(公告)日:1997-12-29
申请号:EP92918087
申请日:1992-08-05
申请人: MOBIL OIL CORP
发明人: APELIAN MINAS ROBERT , COLLINS NICK ALLEN , DEGNAN THOMAS FRANCIS JR , FLETCHER DAVID LEE , HARANDI MOHSEN NADIMI , HILBERT TIMOTHY LEE , KONDIS EDWARD FRANK , MCGOVERN STEPHEN JAMES , OWEN HARTLEY , SHIH STUART , SARLI MICHAEL SEBASTIAN
IPC分类号: C10G35/04 , B01J29/40 , B01J29/70 , B01J37/00 , C10G35/095 , C10G63/02 , C10G69/02 , C10G69/08
CPC分类号: C10G69/08 , B01J29/40 , B01J29/70 , B01J37/0009
摘要: Low sulfur gasoline of relatively high octane number is produced from a catalytically cracked, sulfur-containing naphtha by hydrodesulfurisation followed by treatment over an acidic catalyst, preferably an intermediate pore size zeolite such as ZSM-5. The treatment over the acidic catalyst in the second step restores the octane loss which takes place as a result of the hydrogenative treatment and results in a low sulfur gasoline product with an octane number comparable to that of the feed naphtha. A catalytically cracked naphtha from the FCC main column (10) is first hydrotreated in a hydrotreater (11) which it enters through inlet (12). From hydrotreater (11), the desulfurised naphtha passes through line (13) to the second reactor (14) in which it is contacted with ZSM-5 or another acidic catalyst, for example zeolite beta or MCM-22 where a controlled degree of cracking takes place with an octane, which was lost in the hydrotreater, being restored. The effluents from reactor (14) are separated and further processed.
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公开(公告)号:EP0799082A4
公开(公告)日:1998-12-30
申请号:EP95941486
申请日:1995-12-02
申请人: MOBIL OIL CORP
发明人: APELIAN MINAS ROBERT , BORGHARD WILLIAM STERN , DEGNAN THOMAS FRANCIS , HANLON ROBERT TRYON , RUBIN MAE KOENIG
IPC分类号: C10G45/64 , C10G47/12 , C10G49/02 , C10G65/02 , C10G65/04 , C10G65/12 , C10G67/04 , C10G71/00 , C10G73/06 , C10G73/44 , B01B1/00
CPC分类号: C10G45/64
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公开(公告)号:EP0641375A4
公开(公告)日:1995-04-26
申请号:EP92918087
申请日:1992-08-05
申请人: MOBIL OIL CORP
发明人: APELIAN MINAS ROBERT , COLLINS NICK ALLEN , DEGNAN THOMAS FRANCIS JR , FLETCHER DAVID LEE , HARANDI MOHSEN NADIMI , HILBERT TIMOTHY LEE , KONDIS EDWARD FRANK , MCGOVERN STEPHEN JAMES , OWEN HARTLEY , SHIH STUART SHAN-SAN , SARLI MICHAEL SEBASTIAN
IPC分类号: C10G35/04 , B01J29/40 , B01J29/70 , B01J37/00 , C10G35/095 , C10G63/02 , C10G69/02 , C10G69/08
CPC分类号: C10G69/08 , B01J29/40 , B01J29/70 , B01J37/0009
摘要: Low sulfur gasoline of relatively high octane number is produced from a catalytically cracked, sulfur-containing naphtha by hydrodesulfurisation followed by treatment over an acidic catalyst, preferably an intermediate pore size zeolite such as ZSM-5. The treatment over the acidic catalyst in the second step restores the octane loss which takes place as a result of the hydrogenative treatment and results in a low sulfur gasoline product with an octane number comparable to that of the feed naphtha. A catalytically cracked naphtha from the FCC main column (10) is first hydrotreated in a hydrotreater (11) which it enters through inlet (12). From hydrotreater (11), the desulfurised naphtha passes through line (13) to the second reactor (14) in which it is contacted with ZSM-5 or another acidic catalyst, for example zeolite beta or MCM-22 where a controlled degree of cracking takes place with an octane, which was lost in the hydrotreater, being restored. The effluents from reactor (14) are separated and further processed.
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公开(公告)号:EP0641257A4
公开(公告)日:1994-07-05
申请号:EP92916832
申请日:1992-07-23
申请人: MOBIL OIL CORP
发明人: APELIAN MINAS ROBERT , DEGNAN THOMAS FRANCIS JR , LEONOWICZ MICHAEL EDWARD , KRESGE CHARLES THEODORE , MARLER DAVID OWEN , MAZZONE DOMINICK NICHOLAS , ROTH WIESLAW JERZY , VARTULI JAMES CLARKE
IPC分类号: B01J29/06 , B01J29/03 , B01J29/04 , B01J29/068 , B01J29/076 , B01J29/08 , B01J29/10 , B01J29/83 , B01J29/85 , C10G45/12 , C10G47/16 , C10G47/20 , C10G11/05
CPC分类号: C10G47/16 , B01J29/041 , B01J29/043 , B01J29/044 , B01J29/045 , B01J29/084 , B01J29/10 , B01J29/83 , B01J29/85 , B01J2229/42
摘要: A catalytic composition comprises a metal hydrogenation-dehydrogenation component supported on a support material comprising an ultra-large pore crystalline material of high surface area and porosity. The crystalline material exhibits unusually large sorption capacity demonstrated by its benzene adsorption capacity of greater than about 15 grams benzene/100 grams at 50 torr and 25 °C, and has uniformly sized pores with a maximum perpendicular cross section of at least about 13 Å. In a preferred form, the support material, which is preferably a metallosilicate such as an aluminosilicate, has the pores in a hexagonal arrangement, giving rise to a hexagonal electron diffraction pattern that can be indexed with a d100 value greater than about 18 Å. The catalytic composition is useful in petroleum refining, e.g. hydrocracking of mineral oil feedstocks.
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