Combination coking and hydroconversion process
    1.
    发明授权
    Combination coking and hydroconversion process 失效
    组合焦化和加氢转化过程

    公开(公告)号:US4882036A

    公开(公告)日:1989-11-21

    申请号:US291390

    申请日:1988-12-27

    摘要: A hydrocarbonaceous feed, such as petroleum vacuum distillation bottoms, is upgraded by a combination coking and catalytic slurry hydroconversion process wherein a bottoms fraction from coking is passed through a microfiltration system to remove coke fines, the filtrate passed to a slurry hydroconversion zone, and the bottoms fraction from the slurry hydroconversion zone is also passed through a microfiltration system to remove catalyst particles.

    摘要翻译: 通过组合焦化和催化浆料加氢转化方法提高烃类进料,例如石油真空蒸馏塔底馏分,其中焦化的塔底馏分通过微量过滤系统以除去焦炭,滤液通过浆料加氢转化区, 来自浆料加氢转化区的塔底馏分也通过微量过滤系统以除去催化剂颗粒。

    Process for the desulfurization of heavy oils and bitumens
    6.
    发明授权
    Process for the desulfurization of heavy oils and bitumens 有权
    重油和沥青脱硫工艺

    公开(公告)号:US07862708B2

    公开(公告)日:2011-01-04

    申请号:US12287744

    申请日:2008-10-14

    IPC分类号: C10G45/04

    CPC分类号: C10G45/02 C10G19/02

    摘要: The present invention relates to a process for desulfurizing bitumen and other heavy oils such as low API gravity, high viscosity crudes, tar sands bitumen, or shale oils with alkali metal compounds under conditions to promote in-situ regeneration of the alkali metal compounds. The present invention employs the use of superheated water and hydrogen under conditions to improve the desulfurization and alkali metal hydroxide regeneration kinetics at sub-critical temperatures.

    摘要翻译: 本发明涉及一种在碱性金属化合物的原位再生条件下使沥青和其它重油如API重力低,高粘度原油,焦油砂沥青或页岩油脱硫的方法。 本发明使用过热水和氢气条件来改善亚临界温度下的脱硫和碱金属氢氧化物再生动力学。

    Integrated catalytic cracking and olefin producing process using staged
backflow regeneration
    9.
    发明授权
    Integrated catalytic cracking and olefin producing process using staged backflow regeneration 失效
    综合催化裂化和烯烃生产过程使用分级回流再生

    公开(公告)号:US5447622A

    公开(公告)日:1995-09-05

    申请号:US154828

    申请日:1993-11-19

    CPC分类号: C10G57/00 C10G11/18

    摘要: Disclosed is a method which combines catalytic cracking and olefin production using a coked catalytic cracking catalyst as a dehydrogenation catalyst to dehydrogenate an alkane feed stream and form an olefin rich product stream. The method uses a staged backmixed regeneration system to form the dehydrogenation catalyst and to fully reactivate deactivated cracking catalyst for reuse in the cracking reaction. The catalyst preferably comprises a crystalline tetrahedral framework oxide component.

    摘要翻译: 公开了一种使用焦化催化裂化催化剂作为脱氢催化剂将催化裂化和烯烃生产组合以使烷烃进料流脱氢并形成富烯烃产物流的方法。 该方法使用分级回混再生系统形成脱氢催化剂,并在破裂反应中完全还原失活的裂化催化剂以供再利用。 催化剂优选包含结晶四面体骨架氧化物组分。

    Integrated fluid coking paraffin dehydrogenation process
    10.
    发明授权
    Integrated fluid coking paraffin dehydrogenation process 失效
    综合流体焦化石蜡脱氢工艺

    公开(公告)号:US5435905A

    公开(公告)日:1995-07-25

    申请号:US144984

    申请日:1993-10-27

    摘要: An integrated fluid coking/paraffin dehydrogenation process. The fluid coking unit is comprised of a fluid coker reactor, a heater, and a gasifier. Solids from the fluidized beds are recycled between the coking zone and the heater and between the heater and the gasifier. A separate stream of hot solids from the gasifier is passed to the scrubbing zone after first being reduced in temperature by introduction of an effective amount of diluent, such as steam. A light paraffin stream is introduced into this stream of hot solids between the point where the diluent is added and the scrubbing zone. The hot particles act to catalyze the dehydrogenation of paraffins to olefins.

    摘要翻译: 综合流体焦化/石蜡脱氢工艺。 流体焦化装置由流体焦化反应器,加热器和气化器组成。 来自流化床的固体在焦化区和加热器之间以及加热器和气化器之间循环。 在通过引入有效量的稀释剂如蒸汽首先降低温度后,来自气化器的单独的热固体物流被传送到洗涤区。 在添加稀释剂的点和洗涤区之间,将轻质石蜡流引入该热固体物流中。 热颗粒起催化链烷烃脱氢成烯烃作用。