HEAT EXCHANGER WITH VARYING CROSS SECTIONAL AREA OF CONDUITS
    12.
    发明申请
    HEAT EXCHANGER WITH VARYING CROSS SECTIONAL AREA OF CONDUITS 审中-公开
    热交换器与变化的交叉区域

    公开(公告)号:WO2006120027A1

    公开(公告)日:2006-11-16

    申请号:PCT/EP2006/004550

    申请日:2006-05-15

    Inventor: ASHE, Robert

    Abstract: A process involving heat exchange that employs heat exchangers where the process material flows over a heat transfer surface in which a process material passes through the process conduit of a heat exchanger wherein the desired velocity profile of the process material passing through the process conduit is achieved by varying the cross sectional area of the process conduit in 3 or more locations along the path length of the process conduit which allows better regulation of heating or cooling within the system which, for some processes, will result in improved temperature control.

    Abstract translation: 一种涉及热交换的方法,其使用热交换器,其中工艺材料流过传热表面,其中工艺材料通过热交换器的工艺管道,其中通过过程管道的工艺材料的期望速度分布通过 沿着过程管道的路径长度在3个或更多个位置改变过程管道的横截面积,这允许更好地调节系统内的加热或冷却,这对于一些过程将导致改进的温度控制。

    REDUCED VOLUME HEAT EXCHANGERS
    13.
    发明申请
    REDUCED VOLUME HEAT EXCHANGERS 审中-公开
    减少体积换热器

    公开(公告)号:WO2004017007A3

    公开(公告)日:2004-08-05

    申请号:PCT/EP0308942

    申请日:2003-08-08

    Abstract: A heat exchanger for delivery of heat transfer fluid to a process heat transfer surface is provided, the heat exchanger is in contact with a process fluid and the heat transfer surface comprises at least five heat transfer conduits each having a cross sectional area for the flow path of less than 2000 square millimetres wherein the linear velocity of the heat transfer fluid through the heat transfer conduits is from 0.5 to 20 m.s and adapted so that the temperature of the heat transfer fluid changes by at least 1 °C when they system is operating at design load, the exchanger enables more accurate temperature measurement and control in physical and chemical reactions. Also provided is a heat transfer system in which the heat transfer conduit for passage of the heat transfer fluid is attached to an expansion plate which is in contact with the heat transfer surface and enables independent movement of the heat transfer conduit and the heat transfer surface as their temperature change due to changes in temperature and/or pressure.

    Abstract translation: 提供了一种用于将传热流体输送到工艺传热表面的热交换器,热交换器与工艺流体接触,传热表面包括至少五个传热管道,每个传热管道具有用于流动路径的横截面积 小于2000平方毫米,其中通过传热管道的传热流体的线速度为0.5至20ms -1,并且适于使得当传热流体的温度变化至少1℃时 系统在设计负载下运行,交换器可以在物理和化学反应中实现更准确的温度测量和控制。 还提供了一种传热系统,其中用于传热流体通过的传热管道附接到与传热表面接触的膨胀板,并且能够独立地将传热管道和传热表面移动为 它们的温度由于温度和/或压力的变化而变化。

    FLOW REACTOR WITH EXTENDED FLOW PATH
    14.
    发明申请
    FLOW REACTOR WITH EXTENDED FLOW PATH 审中-公开
    具有扩展流路的流动反应器

    公开(公告)号:WO2014068013A3

    公开(公告)日:2014-08-07

    申请号:PCT/EP2013072742

    申请日:2013-10-30

    Inventor: ASHE ROBERT

    Abstract: A tubular reactor provided with means whereby the tube may be rotated through reciprocating arcs about the longitudinal axis of the tube to provide radial mixing combined with plug flow wherein process material continuously passes through the tubular reactor operating at predetermined reaction conditions and the path of the process material through the rector is diverted from axial flow preferably by means of static and/or dynamic agitators provided within the tubular reactor in order to increase path length, increase process material flow velocity and improve plug flow.

    Abstract translation: 一种管式反应器,其具有使管可以围绕管的纵向轴线旋转的往复式电弧的装置,以提供与塞流相结合的径向混合,其中处理材料连续地通过在预定反应条件下操作的管式反应器和工艺路径 优选通过设置在管式反应器内的静态和/或动态搅拌器将来自反应器的物料从轴流中转移出来,以增加路径长度,提高处理物料流速并改善活塞流量。

    FLOW REACTOR WITH EXTENDED FLOW PATH
    15.
    发明申请
    FLOW REACTOR WITH EXTENDED FLOW PATH 审中-公开
    流动反应器与扩展的流程

    公开(公告)号:WO2014068013A2

    公开(公告)日:2014-05-08

    申请号:PCT/EP2013/072742

    申请日:2013-10-30

    Inventor: ASHE, Robert

    Abstract: A tubular reactor provided with means whereby the tube may be rotated through reciprocating arcs about the longitudinal axis of the tube to provide radial mixing combined with plug flow wherein process material continuously passes through the tubular reactor operating at predetermined reaction conditions and the path of the process material through the rector is diverted from axial flow preferably by means of static and/or dynamic agitators provided within the tubular reactor in order to increase path length, increase process material flow velocity and improve plug flow.

    Abstract translation: 一种管式反应器,其具有这样的装置,其中管可以围绕管的纵向轴线旋转通过往复弧,以提供与塞流结合的径向混合,其中工艺材料连续地通过在预定反应条件下操作的管式反应器和工艺路径 通过反应器的材料优选地通过设置在管式反应器内的静态和/或动态搅拌器从轴向流转向,以增加路径长度,增加工艺材料流速并改善塞子流动。

    IMPROVED MONITORING SYSTEM
    16.
    发明申请
    IMPROVED MONITORING SYSTEM 审中-公开
    改进的监测系统

    公开(公告)号:WO2008064792A1

    公开(公告)日:2008-06-05

    申请号:PCT/EP2007/009970

    申请日:2007-11-19

    Inventor: ASHE, Robert

    CPC classification number: G01N25/18

    Abstract: The use for maintaining good equipment performance for heat transfer equipment which utilises real time heat transfer coefficient measurements to determine the thermal profile between the heat transfer fluid and the process fluid and this is used to maintain a safe operating temperature of the heating/cooling jacket.

    Abstract translation: 用于为传热设备保持良好的设备性能,其利用实时传热系数测量来确定传热流体和过程流体之间的热分布,并且这用于维持加热/冷却套管的安全工作温度。

    CRYSTALLISATION CONTROL METHOD
    17.
    发明申请

    公开(公告)号:WO2008058759A3

    公开(公告)日:2008-05-22

    申请号:PCT/EP2007/009972

    申请日:2007-11-19

    Inventor: ASHE, Robert

    Abstract: A system for controlling crystallisation processes which uses heat measurement for controlling crystal growth wherein the required rate of heating or cooling the product after nucleation is set in a series of steps according the enthalpy of crystallisation as measured in the system.

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