Counter-current flow hollow fiber permeator
    4.
    发明授权
    Counter-current flow hollow fiber permeator 失效
    逆流中空纤维渗透器

    公开(公告)号:US5234591A

    公开(公告)日:1993-08-10

    申请号:US802158

    申请日:1991-12-04

    Abstract: A hollow fiber permeator is described which permits counter-current flow in the passage of feed/retentate and permeate-sweep streams. The permeator comprises a bundle of hollow fibers compartmentalized using a series of concentric shells or a spiral wrap extending the entire length of the hollow fibers. The rings or spiral wrap are perforated along the top and bottom to permit even flow distribution through each of the compartments defined by the concentric rings or spiral wrap so that the linear flow rate down the length of the permeator is similar for each compartment.

    Abstract translation: 描述了一种中空纤维渗透器,其允许在进料/渗余物和渗透物流的通道中产生逆流流动。 渗透器包括一束使用一系列同心壳分隔的中空纤维,或一个延伸整个中空纤维长度的螺旋卷。 环或螺旋卷绕物沿着顶部和底部穿孔以允许均匀的流动分布通过由同心环或螺旋包裹物限定的每个隔间,使得沿着渗透器的长度的线性流速对于每个隔室是相似的。

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

    公开(公告)号:US4765882A

    公开(公告)日:1988-08-23

    申请号:US857358

    申请日:1986-04-30

    CPC classification number: C10G49/12 C10G65/10

    Abstract: A slurry catalytic hydroconversion process comprising at least two hydroconversion zones is provided in which the heavy hydrocarbonaceous fresh oil feed is added to more than one hydroconversion zone. Additional portions of catalysts or catalyst precursors are also added to the first hydroconversion zone and to additional hydroconversion zones.

    Abstract translation: 提供了包含至少两个加氢转化区的淤浆催化加氢转化方法,其中将重质烃类新鲜油进料加入多于一个加氢转化区。 催化剂或催化剂前体的另外部分也加入到第一加氢转化区和另外的加氢转化区。

    Magnetically stabilized, fluidized beds
    7.
    发明授权
    Magnetically stabilized, fluidized beds 失效
    磁稳定,流化床

    公开(公告)号:US4292171A

    公开(公告)日:1981-09-29

    申请号:US131853

    申请日:1980-03-19

    CPC classification number: C10G11/18 B01J8/42

    Abstract: A hydrocarbon conversion process wherein a hydrocarbon feedstock is contacted with a magnetically stabilized fluid bed of particulate solids comprising a mixture of separate, discrete (a) magnetizable substantially non-catalytic particles, and (b) non-magnetizable catalytic particles. The particulate solids mixture is withdrawn from the magnetically stabilized, fluidized bed and separated into magnetizable, substantially non-catalytic particles and non-magnetizable catalyst particles. The non-magnetizable catalytic particles are thereafter regenerated and returned to the hydrocarbon conversion zone. The separated magnetizable, substantially non-catalytic particles are subjected to heat transfer prior to their return to the conversion zone.

    Abstract translation: 一种烃转化方法,其中烃原料与磁性稳定的颗粒固体的流化床接触,其包含单独的,离散的(a)可磁化的基本上非催化的颗粒的混合物,和(b)不可磁化的催化颗粒。 将颗粒状固体混合物从磁稳定的流化床中取出并分离成可磁化的,基本上不催化的颗粒和不可磁化的催化剂颗粒。 此后,不可磁化的催化剂颗粒再生并返回烃转化区。 分离的可磁化的,基本上不催化的颗粒在返回到转化区之前经受热传递。

    Heat transfer in magnetically stabilized, fluidized beds
    9.
    发明授权
    Heat transfer in magnetically stabilized, fluidized beds 失效
    在磁稳定的流化床中传热

    公开(公告)号:US4294688A

    公开(公告)日:1981-10-13

    申请号:US131855

    申请日:1980-03-19

    Inventor: Francis X. Mayer

    CPC classification number: C10G49/16 B01J8/26 B01J8/42 C10G11/18 C10G15/00

    Abstract: Heat transfer in a hydrocarbon conversion process utilizing a magnetically stabilized fluid bed reactor and a magnetically stabilized catalyst regenerator is improved by the use of a fluidizable solids mixture comprising substantially inert heat carrier particles and magnetizable catalyst particles wherein the inert particles have settling rates higher than the settling rates of the catalyst particles. The heat carrier particles and the magnetizable catalyst particles are completely or partially separated in settling zones associated with the reactor and regenerator. The separated heat carrier particles and catalyst particles are independently circulated between the reactor and regenerator so that the heat carrier particles can be passed through one or more heat exchangers to provide the desired temperature levels in the system.

    Abstract translation: 通过使用包含基本上惰性的载热颗粒和可磁化的催化剂颗粒的可流化的固体混合物,利用磁稳定的流化床反应器和磁稳定的催化剂再生器在烃转化过程中进行热转移,其中惰性颗粒的沉降速率高于 催化剂颗粒的沉降速率。 热载体颗粒和可磁化催化剂颗粒在与反应器和再生器相关联的沉降区域中完全或部分分离。 分离的载体颗粒和催化剂颗粒在反应器和再生器之间独立地循环,使得载体颗粒可以通过一个或多个热交换器以在系统中提供期望的温度水平。

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