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    HEAT EXCHANGE CATALYTIC REACTOR
    12.
    发明申请
    HEAT EXCHANGE CATALYTIC REACTOR 审中-公开
    热交换催化反应器

    公开(公告)号：WO1997025136A1

    公开(公告)日：1997-07-17

    申请号：PCT/GB1996002999

    申请日：1996-12-06

    Applicant: IMPERIAL CHEMICAL INDUSTRIES PLC ,  CREWDSON, Bernard, John

    Inventor： IMPERIAL CHEMICAL INDUSTRIES PLC

    IPC: B01J08/06

    CPC classification number: F28F9/22 ,  B01J8/067 ,  B01J2208/0007 ,  B01J2208/00088 ,  B01J2208/00212 ,  Y10S165/401

    Abstract: A heat exchange catalytic process and reactor of the shell-and-tube type having a plurality of tubes extending longitudinally through the shell from a tube fluid inlet region to a tube fluid outlet region and baffles extending transversely across the shell dividing the shell between said inlet and outlet regions into at least three heat exchange zones through which each tube passes in sequence in heat exchange with that zone. A shell fluid is passed through the heat exchange zones in heat exchange with the tube fluid passing through the tubes. Transfer passages are provided connencting the heat exchange zones and are disposed so that the shell fluid passes through the second zone before or after it has passed through both the first and third zones. A particulate catalyst is disposed in either the shell heat exchange zones or, preferably, the tubes. The process utilises a heat exchange medium, particularly water, that does not change state under the prevailing conditions and is preferably fed to the shell heat exchange zones while the reactant stream passes through the catalyst disposed in the tubes. The process is particularly applicable to the selective hydrogenation of acetylenes in the presence of olefins.

    Abstract translation: 壳管式热交换催化过程和反应器，其具有多个管，其从管流体入口区域纵向延伸穿过壳体到管流体出口区域，横向穿过壳体延伸的挡板，所述壳体在所述入口 和出口区域分成至少三个热交换区，每个管通过该区域依次与该区域热交换。 壳体流体通过与通过管的管流体热交换的热交换区。 提供与热交换区域相连接的转移通道，并且设置成使得壳体流体在其通过第一和第三区域之前或之后通过第二区域。 颗粒催化剂设置在壳体热交换区域中，或优选地设置在管道中。 该方法利用在主要条件下不改变状态的热交换介质，特别是水，并且优选在反应物流通过设置在管中的催化剂的同时进料到壳体热交换区。 该方法特别适用于乙烯在烯烃存在下的选择性氢化。

    CATALYTIC REACTOR FOR ENDOTHERMIC REACTIONS
    13.
    发明申请
    CATALYTIC REACTOR FOR ENDOTHERMIC REACTIONS 审中-公开
    催化反应器的吸热反应

    公开(公告)号：WO1995011745A1

    公开(公告)日：1995-05-04

    申请号：PCT/DE1994001293

    申请日：1994-10-26

    Applicant: MANNESMANN AG ,  K.T.I. Group B.V. ,  GIACOBBE, Francesco

    Inventor： MANNESMANN AG ,  K.T.I. Group B.V.

    IPC: B01J08/06

    CPC classification number: C01B3/384 ,  B01J8/062 ,  B01J2208/00495 ,  B01J2219/00157 ,  C01B2203/0811 ,  C01B2203/0816 ,  C01B2203/0844 ,  C01B2203/0866

    Abstract: A catalytic reactor for endothermic reactions is disclosed. The catalyst is located in a housing (13) made of refractory material, and at least a tubular catalyst vessel (10) is arranged inside the housing (13). In order to obtain a catalytic reactor that avoids thermal damages to the reactor vessel without requiring costly construction measures nor undesirable increases in the amounts of exhaust gasses, as well as the resulting inconveniences for the energy efficiency of the fuels used, several mutually spaced catalyst vessels (10) are arranged in the housing (13), a plurality of burners (15) is arranged in the housing (13) in such a way that the catalyst vessels (10) lie between the burners (15) and the flame area of the burners (15) lies in the area of the heat dissipators (16) in order to ensure a non-adiabatic combustion.

    Abstract translation: 本发明涉及一种用于吸热反应的催化反应器。 催化剂位于从耐火材料壳体（13）形成的载体，其中，所述壳体（13）的至少一个管状催化剂容器（10）的内部布置。 为了提供在其中避免了反应器容器的热损伤，而不主要建筑工作或在废气和所使用的燃料的能量利用率缺点的量不希望有的增加必须被考虑到催化反应器，本发明提出的是，在壳体（13）的每个 彼此的多个催化剂容器（10）被布置在所述壳体间隔开（13）包括多个燃烧器（15）被布置在这样一种方式，燃烧器之间的催化剂容器（10）（15）位于与所述燃烧器的火焰区域 （15），以确保在热分配器（16）的区域中的每个情况下，非绝热燃烧。

    Vertical tube reactor with serial downward flow through a plurality of sets of particulate containing tubes
    16.
    发明公开
    Vertical tube reactor with serial downward flow through a plurality of sets of particulate containing tubes 失效
    垂直管式反应器，通过多个包含颗粒的管子组成一系列下行流程

    公开(公告)号：EP0200990A3

    公开(公告)日：1987-05-20

    申请号：EP86105581

    申请日：1986-04-22

    Applicant: UOP INC.

    Inventor： Ward, Dennis John

    IPC: B01J08/06 ,  C07C02/08

    CPC classification number: B01J8/06 ,  B01J2208/00212 ,  B01J2208/0069 ,  Y10T29/49826

    Abstract: A single pass, shell and tube reactor which is designed for downflow of reactant fluid in tubes containing contact material is improved to allow more than one downflow pass of fluid through the tubes by providing upper and lower vertically aligned partition members to divide the upper and lower tube end chambers into isolated compartments and by using an empty tube to allow upflow communication between adjacent compartments. In a two compartment configuration, the upper and lower tube end chambers are each partitioned in half, but the lower partition member has a screened port to allow fluid from the first compartment to reach, and move upwardly through, an empty tube(s) in the second compartment which is isolated from the other tubes in the second compartment at its bottom end but not at its top end.

    Process for production of ethylene oxide and reactor suitable therefor
    17.
    发明公开
    Process for production of ethylene oxide and reactor suitable therefor 失效
    生产乙烯氧化物及其适用的反应器的方法

    公开(公告)号：EP0130807A3

    公开(公告)日：1986-04-23

    申请号：EP84304422

    申请日：1984-06-28

    Applicant: THE HALCON SD GROUP, INC.

    Inventor： Ozero, Brian J. ,  Becker, Stanley D.

    IPC: C07D301/10 ,  C07D303/04 ,  B01J08/06

    CPC classification number: C07D301/10 ,  B01J8/06 ,  B01J8/067

    Abstract: Improved performance is obtained in a multi-tube reactor for oxidation of ethylene to ethylene oxide by providing a distribution zone for the coolant located downstream of the catalyst and a contiguous cooling zone. The effluent gases from the oxidation are cooled in the cooling zone by a fluid, which has been only slightly preheated and distributed uniformly in the distribution zone by contact with tubes in which the effluent gases are in low-turbulence flow. Uniform distribution of the coolant provides substantially equal cooling of the effluent gases in each tube, thus minimizing the variation in effluent gas temperature among the tubes. Preferably, the tubes in the cooling section are packed with inert particles to facilitate heat transfer, while the tubes are empty in the distribution section to reduce heat transfer.

    Abstract translation: 在用于将乙烯氧化成环氧乙烷的多管反应器中获得改进的性能，通过为位于催化剂下游的冷却剂和连续的冷却区域提供分配区。 来自氧化的流出气体在冷却区中被流体冷却，该流体仅通过与流出气体处于低湍流的管接触而略微预热并均匀分布在分配区中。 冷却剂的均匀分布为每个管中的流出气体提供了基本上相等的冷却，从而最小化了管中流出气体温度的变化。 优选地，冷却部分中的管装有惰性颗粒以促进热传递，而管在分配部分中是空的，以减少热传递。

    Reactor temperature control systems
    18.
    发明公开
    Reactor temperature control systems 失效
    反应器温度控制系统

    公开(公告)号：EP0094208A3

    公开(公告)日：1985-07-10

    申请号：EP83302539

    申请日：1983-05-05

    Applicant: THE BABCOCK & WILCOX COMPANY

    Inventor： Agarwal, Suresh C.

    IPC: B01J08/06 ,  C07D301/08

    CPC classification number: B01J8/06 ,  B01J8/001 ,  B01J8/067 ,  B01J2208/00008 ,  B01J2208/00044 ,  B01J2208/00088 ,  B01J2208/00097 ,  B01J2219/0006 ,  B01J2219/00069 ,  B01J2219/00085 ,  C07D301/08 ,  Y02P20/142

    Abstract: A temperature control system controls the temperature of an olefin oxidation reactor (10) by measuring various parameters in the reactor and in flow lines to and from the reactor, and using these parameters with known quantities for specific heat of the feed and effluent and heats of vaporization and reaction, to calculate a coolant flow rate set point. Parameters relating to the heat balance with regard to a desired olefin oxide product and undesired carbon dioxide products are utilized for correct control. Equipment is also provided for ascertaining the state of a catalyst used in the reaction. Circuit components are provided for obtaining changes in flow rates, temperatures and concentrations to calculate a change in coolant flow rate as well as the steady state effluent flow rate quantity to improve the system response to start up, shut down and transient conditions.

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