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108 条记录 (耗时 0.015 秒)

    Conversion of light hydrocarbons to ether rich gasolines
    3.
    发明公开
    Conversion of light hydrocarbons to ether rich gasolines 失效
    在Ether enthaltende Benzine的Umwandlung von lichten Kohlenwasserstoffen。

    公开(公告)号：EP0509162A1

    公开(公告)日：1992-10-21

    申请号：EP91303339.5

    申请日：1991-04-16

    申请人： MOBIL OIL CORPORATION (a New York corporation)

    发明人： Bell, Weldon Kay ,  Haag, Werner Otto ,  Harandi, Mohsen Nadimi ,  Owen, Hartley

    IPC分类号： C10L1/02

    CPC分类号： C10L1/023 ,  Y02P30/20

    摘要： A process is disclosed for converting a light hydrocarbon feedstock that contains a mixture of linear and branched olefins to ether-rich high octane gasoline streams that include tertiary alkyl and isoalkyl ethers such as MTBE, TAME, methyl isopropyl ether (MIPE), and methyl sec-butylether (MSBE). The process involves initially etherifying the tertiary olefins with a lower alcohol in the presence of an ion exchange resin catalyst, and then etherifying the linear olefins in the presence of a zeolite catalyst, such as zeolite beta. The unreacted olefins from the etherification reactions are converted to gasoline boiling range hydrocarbons by oligomerization with a zeolite catalyst, such as ZSM-5.

    摘要翻译： 公开了一种将包含直链和支链烯烃混合物的轻质烃原料转化成富含高级辛烷值汽油的方法，其中包括叔烷基和异烷基醚如MTBE，TAME，甲基异丙醚（MIPE）和甲基sec 丁基醚（MSBE）。 该方法首先在离子交换树脂催化剂的存在下用低级醇醚化叔烯烃，然后在沸石催化剂如沸石β存在下醚化直链烯烃。 来自醚化反应的未反应烯烃通过用沸石催化剂如ZSM-5低聚转化成汽油沸程烃。

    Production of aromatics-rich gasoline with low benzene content
    7.
    发明公开
    Production of aromatics-rich gasoline with low benzene content 失效
    维尔法赫恩·赫斯特伦

    公开(公告)号：EP0414449A1

    公开(公告)日：1991-02-27

    申请号：EP90309026.4

    申请日：1990-08-16

    申请人： MOBIL OIL CORPORATION

    发明人： Harandi, Mohsen Nadimi ,  Owen, Hartley

    IPC分类号： C10G59/02 ,  C10L1/06

    CPC分类号： C10G63/00 ,  C10L1/06

    摘要： A process for the production of high octane gasoline rich in aromatics but containing a relatively low concentration of benzene comprises the separation of C₆ fraction of the gasoline feedstock into n-hexane and other C₆ isomers. The n-hexane and C₇+ streams are catalytically reformed to produce a reformate with a diminished yield of benzene. The reformate is separated and the C₆- reformate fraction containing benzene is alkylated employing a zeolite catalyst such as ZSM-5 and preferably methanol or propylene as the alkylating agent. The alkylate comprises high octane C₇+ alkylaromatics.

    摘要翻译： 生产富含芳烃但含有较低浓度苯的高辛烷值汽油的方法包括将汽油原料的C6馏分分离成正己烷和其他C6异构体。 对正己烷和C 7 +流进行催化重整以产生苯的产率降低的重整产物。 分离重整产物，使用沸石催化剂如ZSM-5，优选甲醇或丙烯作为烷基化剂，将含有苯的C6重整油馏分烷基化。 烷基化物包括高辛烷值C7 +烷基芳族化合物。

    Solids-gas separator
    8.
    发明公开
    Solids-gas separator 失效
    固体气体分离器

    公开(公告)号：EP0262916A3

    公开(公告)日：1990-03-07

    申请号：EP87308595.5

    申请日：1987-09-29

    申请人： MOBIL OIL CORPORATION

    发明人： Haddad, James Henry ,  Owen, Hartley

    IPC分类号： B04C5/28 ,  C10G11/18

    CPC分类号： C10G11/182 ,  B01D45/12 ,  B01J8/0055 ,  B04C5/28 ,  B04C9/00

    摘要： A catalyst recovery apparatus is provided for separating finely divided solid particles from a hot gas stream comprising a vertical metal shell having a lower hot gas inlet and an upper clean gas outlet, a plurality of thermally expandable metal cyclone assemblies supported at their top regions by a horizontal plate, each of the cyclone assemblies having a downwardly extending dip-leg which exits into a centrally disposed solids collector, a vertically slidable particle collector outlet conduit which extends from the collector bottom downwardly through the enclosed shell, and a compressible seal means or packing gland arrangement disposed around the collector outlet conduit and comprising an annular packing holder member, a vertically movable packing compression member, and a compressible packing material.

    Two-stage process for converson of alkanes to gasoline
    9.
    发明公开
    Two-stage process for converson of alkanes to gasoline 无效
    烷烃转化为汽油的两阶段工艺

    公开(公告)号：EP0325438A3

    公开(公告)日：1989-10-25

    申请号：EP89300467.1

    申请日：1989-01-18

    申请人： MOBIL OIL CORPORATION

    发明人： Harandi, Mohsen Nadimi ,  Owen, Hartley

    IPC分类号： C10G57/02

    CPC分类号： C10G11/182 ,  C10G57/02 ,  Y10S585/91

    摘要： Lower alkanes are converted to olefins in a 'third bed' external catalyst cooler (ECC) in which hot catalyst, from a first regenerator ('second best') operating in conjunction with a fluid catalytic cracker ('first bed'), thermally cracks and dehydrogenates the alkanes. Because this is an endothermic reaction, the catalyst is autogeneously cooled before it is recirculated to the FCC regenerator. The cracking catalyst is the catalyst of choice in the FCC reactor. Maximum conversion of alkanes to olefins is sought, and can be maintained because the FCC regenerator burns the coke made during alkane dehydrogenation. The olefins produced are then oligomerized in an oligomerization reactor ("fourth" bed) operating in conjunction with a second regenerator ("fifth" bed) to produce a gasoline range stream. The interrelataed operation of this combination of five fluid beds is tailored to convert all available low value alkanes, to olefins which are generally in high demand for several uses, particularly to make high value gasoline.