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    Upgrading light olefins in a turbulent fluidized catalyst bed reactor
    4.
    发明授权
    Upgrading light olefins in a turbulent fluidized catalyst bed reactor 失效
    在湍流流化催化剂床反应器中升级轻质烯烃

    公开(公告)号：US4746762A

    公开(公告)日：1988-05-24

    申请号：US6407

    申请日：1987-01-23

    申请人： Amos A. Avidan ,  Tai-Sheng Chou ,  Hartley Owen ,  Jorge L. Soto ,  Samuel A. Tabak

    发明人： Amos A. Avidan ,  Tai-Sheng Chou ,  Hartley Owen ,  Jorge L. Soto ,  Samuel A. Tabak

    IPC分类号： B01J8/24 ,  B01J29/40 ,  C07C1/20 ,  C07C2/00 ,  C10G3/00 ,  C10G35/095 ,  C10G50/00 ,  C10G57/02 ,  C07C2/12

    CPC分类号： C07C1/20 ,  B01J29/40 ,  C07C2/00 ,  C10G50/00 ,  B01J2208/00265 ,  B01J2229/42 ,  C07C2529/40 ,  C10G2300/1092 ,  C10G2300/4081 ,  C10G2400/30 ,  Y02P20/52 ,  Y02P30/20

    摘要： A fluidized bed catalytic process for conversion of light olefinic gas feedstock containing ethene to produce hydrocarbons rich in C.sub.5.sup.+ liquids, comprising the steps of maintaining a fluidized bed of zeolite catalyst particles in a turbulent reactor bed at a temperature of about 315.degree. to 510.degree. C., said catalyst having an apparent particle density of about 0.9 to 1.6 g/cm.sup.3 and a size range of about 1 to 150 microns, and average catalyst particles size of about 20 to 100 microns containing about 10 to 25 weight percent of fine particles having a particle size less than 32 microns; passing hot feedstock vapor upwardly through the fluidized catalyst bed under turbulent flow conditions; maintaining turbulent fluidized bed conditions through the reactor bed between transition velocity and transport velocity at a superficial fluid velocity of about 0.3 to 2 meters per second; and recovering hydrocarbon product containing a major amount of C.sub.5.sup.+ hydrocarbons and containing C.sub.3 -C.sub.5 alkanes and alkenes in the ratio of about 0.2:1 to 5:1.

    摘要翻译： 一种用于转化含有乙烯的轻质烯烃气体原料以产生富含C5 +液体的烃的流化床催化方法，包括以下步骤：将沸石催化剂颗粒的流化床在约315℃至510℃的温度下保持在湍流反应器床中 所述催化剂具有约0.9至1.6g / cm 3的表观颗粒密度和约1至150微米的尺寸范围，以及约20至100微米的平均催化剂颗粒尺寸，其含有约10至25重量％的具有 粒度小于32微米; 在湍流条件下将热原料蒸气向上通过流化催化剂床; 保持湍流流化床条件通过反应器床在过渡速度和运输速度之间以约0.3至2米/秒的表面流体速度; 并以约0.2:1至5:1的比例回收含有大量C 5+烃并含有C 3 -C 5烷烃和烯烃的烃产物。

    Hydroconversion process
    6.
    发明授权
    Hydroconversion process 失效
    加氢转化过程

    公开(公告)号：US4997544A

    公开(公告)日：1991-03-05

    申请号：US350865

    申请日：1989-05-12

    申请人： Tai-Sheng Chou ,  Clinton R. Kennedy ,  Stuart S. Shih

    发明人： Tai-Sheng Chou ,  Clinton R. Kennedy ,  Stuart S. Shih

    IPC分类号： C10G65/04 ,  C10G65/10

    CPC分类号： C10G65/04 ,  C10G65/10

    摘要： This invention provides a fixed bed of nonuniformly sized grade catalyst particles for hydrocracking or hydrodesulfurization. The graded particles are arranged with the largest particles in either the upstream or the downstream portion of the bed. In either case, when compared with the conventional bed of uniformly sized particles, the graded bed of this invention shows enhanced hydrocarbon conversion activity for heavy oils over a useful range of conversion. Such catalyst bed is particularly useful in moderate hydrocracking operating at less than 1000 psig (7000 kPa) pressure.

    摘要翻译： 本发明提供了用于加氢裂化或加氢脱硫的不均匀级别的催化剂颗粒的固定床。 分级颗粒在床的上游或下游部分中布置有最大的颗粒。 在任一种情况下，当与常规均匀尺寸的颗粒床相比时，本发明的分级床在有效的转化范围内显示出对重油的烃转化活性的增强。 这种催化剂床在小于1000psig（7000kPa）压力下的中等加氢裂化操作中是特别有用的。

    Inlet distributor for fixed bed catalytic reactor
    9.
    发明授权
    Inlet distributor for fixed bed catalytic reactor 失效
    固定床催化反应器入口分配器

    公开(公告)号：US4788040A

    公开(公告)日：1988-11-29

    申请号：US883848

    申请日：1986-07-10

    申请人： Joseph F. Campagnolo ,  Tai-Sheng Chou ,  William F. Heaney ,  John D. Ruggles

    发明人： Joseph F. Campagnolo ,  Tai-Sheng Chou ,  William F. Heaney ,  John D. Ruggles

    IPC分类号： B01J8/02 ,  C10G49/00 ,  B01D47/00 ,  B01J8/04

    CPC分类号： C10G49/002 ,  B01J8/0278

    摘要： An inlet distributor system for a fixed bed catalyst reactor which includes an inlet deflector cone positioned to deflect liquid in cooperation with a splash plate onto a liquid distributor trough positioned therebelow. An upper tray is positioned beneath the distributor trough to receive liquid therefrom. The upper distributor tray has a series of risers in spaced position thereon and extending above and below the upper distributor tray. The risers are hollow and open above and below the upper distributor tray to permit vapor to pass through the tray and each riser has a plurality of weir slots cut into its outer surface through which liquid can pass through the tray. A lower distributor tray is positioned beneath the upper distributor tray to receive liquid passing through the weir slots of the risers. The lower distributor tray has a series of risers and downpipes thereon arranged in a predetermined pattern. Each of the risers and downpipes in said pattern extend above and below the lower distributor tray and have openings above and below the lower distributor tray to form a through passageway for liquid to pass through the tray when received from the upper distributor tray. The passageway in the downpipes is formed by an axial bore therethrough and the passageway in the risers is formed by its hollow tubular configuration open at the bottom and having a side opening therein above the upper surface of the lower distributor tray each riser includes another upper opening above the lower distributor tray to permit vapor to pass through the tray. The pattern of risers and downpipes provide an advantageous arrangement of passageways for liquid to be distributed to the catalytic bed therebelow.

    摘要翻译： 一种用于固定床催化剂反应器的入口分配器系统，其包括入口偏转器锥体，其定位成将与溅射板协作的液体偏转到位于其下方的液体分配器槽。 上托盘位于分配器槽下方以从其接收液体。 上部分配器托盘具有一系列在隔板位置上的提升器，并且在上部分配器托盘的上方和下方延伸。 上升管是中空的，并且在上部分配器托盘的上方和下方敞开，以允许蒸汽通过托盘，并且每个提升管具有切割到其外表面中的多个堰槽，液体可以通过该外部表面通过托盘。 下部分配器托盘位于上部分配器托盘下方以接收通过提升管的堰槽的液体。 下分配器托盘在其上以预定图案布置有一系列立管和落管。 所述图案中的每个立管和下水管都在下部分配器托盘的上方和下方延伸，并且在下部分配器托盘的上方和下方具有开口，以形成通道，用于在从上部分配器托盘接收时液体通过托盘。 下水管中的通道由穿过其中的轴向孔形成，并且提升管中的通道由其在底部开放的中空管状构造形成，并且在下分配器托盘的上表面上方具有侧开口，每个立管包括另一上部开口 在下分配器托盘上方，以允许蒸汽通过托盘。 提升管和水管的图案提供了用于液体分配到其下方的催化床的通道的有利布置。

    Process scheme for processing sour feed in isomerization dewaxing
    10.
    发明授权
    Process scheme for processing sour feed in isomerization dewaxing 失效
    异构脱蜡酸加工工艺方案

    公开(公告)号：US5906729A

    公开(公告)日：1999-05-25

    申请号：US986781

    申请日：1997-12-08

    申请人： Tai-Sheng Chou

    发明人： Tai-Sheng Chou

    IPC分类号： C10G45/60 ,  C10G45/04 ,  C10G65/02 ,  C10G65/04 ,  C10G69/02

    CPC分类号： C10G65/043

    摘要： This invention is directed to an improved process scheme to process sour feed in the reaction section of the process unit, including isomerization dewaxing with zeolite beta. The instant invention employs countercurrent flow in the fixed bed of the MIDW(Mobil Isomerization Dewaxing) reactor (the reactor in which isomerization dewaxing occurs) with recycle gas being the gas stream in the MIDW bed. With this arrangement hydrodesulfurization(HDS) and MIDW occur in an integrated process.

    摘要翻译： 本发明涉及一种改进的处理装置反应段中酸源的方法，包括用β沸石进行异构脱蜡。 本发明在MIDW床中的气流中使用循环气体的MIDW（Mobil异构化脱蜡）反应器（发生异构化脱蜡的反应器）的固定床中采用逆流流动。 通过这种安排，加氢脱硫（HDS）和MIDW发生在一个整合的过程中。