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    Heat exchange catalytic reactor
    4.
    发明授权
    Heat exchange catalytic reactor 失效
    热交换催化反应器

    公开(公告)号：US6039113A

    公开(公告)日：2000-03-21

    申请号：US101369

    申请日：1998-07-09

    申请人： Bernard John Crewdson

    发明人： Bernard John Crewdson

    IPC分类号： B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  F28F9/22

    CPC分类号： F28F9/22 ,  B01J8/067 ,  B01J2208/0007 ,  B01J2208/00088 ,  B01J2208/00212 ,  Y10S165/401

    摘要： 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.

    摘要翻译： PCT No.PCT / GB96 / 02999第 371日期：1998年7月9日 102（e）日期1998年7月9日PCT 1996年12月6日PCT PCT。 出版物WO97 / 25136 日期1997年7月17日一种管壳式热交换催化工艺和反应器，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，横向延伸穿过壳体分隔件 所述入口区域和出口区域之间的壳体进入至少三个热交换区域，每个管道通过该热交换区域与该区域热交换依次通过。 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。

    Device for cooling hot, dust-laden gases
    5.
    发明授权
    Device for cooling hot, dust-laden gases 失效
    用于冷却热，含尘气体的装置

    公开(公告)号：US4727933A

    公开(公告)日：1988-03-01

    申请号：US903462

    申请日：1986-09-03

    申请人： Eckhard Hell ,  Manfred Forster

    发明人： Eckhard Hell ,  Manfred Forster

    IPC分类号： C10J3/86 ,  C10K1/04 ,  F22B1/18 ,  F22B37/20 ,  F28D7/00 ,  F28D7/08 ,  F28D7/16 ,  F28F9/00 ,  F28F9/013 ,  F22B37/24

    CPC分类号： F28D7/005 ,  C10J3/86 ,  C10K1/04 ,  F22B1/1846 ,  F28F9/013 ,  F28D2021/0075 ,  Y10S165/401

    摘要： A device for cooling hot, compressed, dust-laden gases. The device consists of an inner structure made out of cooled tubes, positioned inside a pressurized container. The device contains several straight partitions made out of tubes. The partitions parallel the longitudinal axis of the inner structure. The object is to redesign the heat-emitting surfaces of the device in order to make it more compact. At least one of the straight partitions is bent out into a nest of tubes. The nest extends through the cross-section of the inner structure. The tubes that the nest is made out of extend through and are supported by the rest of the partitions.

    摘要翻译： 用于冷却热，压缩，含尘气体的装置。 该装置包括由冷却管制成的内部结构，其位于加压容器内。 该装置包含几根直管，由管制成。 分隔件平行于内部结构的纵向轴线。 目的是重新设计器件的发光表面，以使其更紧凑。 至少一个直的分区被弯曲成一个管子。 巢延伸穿过内部结构的横截面。 嵌套的管由延伸穿过并由其余的隔板支撑。

    Construction and method for improving heat transfer and mechanical life of tube-bundle heat exchangers
    6.
    发明授权
    Construction and method for improving heat transfer and mechanical life of tube-bundle heat exchangers 失效
    管束换热器的传热和机械寿命改善的结构和方法

    公开(公告)号：US4708198A

    公开(公告)日：1987-11-24

    申请号：US717580

    申请日：1985-03-29

    申请人： Richard A. Holl

    发明人： Richard A. Holl

    IPC分类号： F28F13/02 ,  F28F13/12

    CPC分类号： F28F13/12 ,  F28D7/16 ,  F28F13/02 ,  Y10S165/401

    摘要： An improved heat exchange construction for tube bundle heat exchange systems including shell (4) and tube (6) types (2), incorporating detached, essentially spherical flow interrupters (24, 26) arranged in an interconnected matrix configuration (22), and disposed within the tube bundle interstices (9, 11). Substantial improvements in heat exchange and exchanger tube life, is provided. The mechanically interconnected matrix configuration of the flow interrupters provides an economical and easily assembled means to improve heat transfer outside of individual tubes in a tube bundle configuration. Continuous tube support is also provided by tube/interrupter contact, thereby greatly decreasing fatigue failures encountered in presently used multiple tube, tube/shell heat exchanger configurations (2).

    摘要翻译： 一种用于管束热交换系统的改进的热交换结构，包括壳体（4）和管（6）类型（2），其包括布置在互连的矩阵构型（22）中的分离的，基本上为球形的流动断流器（24,26），并且设置 在管束间隙（9,11）内。 提供了热交换和换热器管寿命的显着改进。 流动断路器的机械互连矩阵结构提供了一种经济且易于组装的装置，以改善管束构造中各个管外部的传热。 连续管支撑也由管/断续器接触提供，从而大大减少目前使用的多管，管/壳热交换器构造（2）中遇到的疲劳失效。

    Heat exchanger for a gaseous and a liquid medium
    7.
    发明授权
    Heat exchanger for a gaseous and a liquid medium 失效
    用于气体和液体介质的热交换器

    公开(公告)号：US4479536A

    公开(公告)日：1984-10-30

    申请号：US294993

    申请日：1981-08-21

    申请人： Herman J. Lam/e/ ris

    发明人： Herman J. Lam/e/ ris

    IPC分类号： F28D7/00 ,  F28F9/26 ,  F28F19/00 ,  F28F9/22

    CPC分类号： F28F19/00 ,  F28D7/0041 ,  F28F9/26 ,  Y10S165/401

    摘要： A heat exchanger block includes a series of rows of tubes, the end rows of which are joined to form walls, and two further rows of tubes at the opposite sides of the series, also formed as walls. The tubes of the further rows are shorter than the other tubes and, at one side, are spaced downwardly from the top and, at the other side, are spaced upwardly from the bottom. A pair of lateral openings at the opposite sides and ends of the block results. The blocks may be joined to provide composites or they may be separate although joined at one pair of their lateral openings. A pressure vessel may enclose the blocks to relieve them of rupturing pressure.

    摘要翻译： 热交换器块包括一系列管，其端排被连接以形成壁，并且在该系列的相对侧的另外两排管也形成为壁。 另外一排的管子比其他管子短，并且在一侧与顶部间隔开，并且在另一侧与底部间隔开。 在块的相对侧和端部处形成一对侧向开口。 块可以连接以提供复合材料，或者它们可以是分开的，尽管在其一对侧开口处接合。 压力容器可以封闭块以减轻它们的破裂压力。

    Heat transfer structure
    10.
    发明授权
    Heat transfer structure 失效
    热传递结构

    公开(公告)号：US3704748A

    公开(公告)日：1972-12-05

    申请号：US3704748D

    申请日：1970-02-11

    申请人： RATHEON CO

    发明人： HAPGOOD WILLIAM H

    IPC分类号： F22B37/04 ,  F22B37/10 ,  F24H1/14 ,  F24H1/16 ,  F28D7/02 ,  F28D7/16 ,  F28F1/10 ,  F28F13/00

    CPC分类号： F28D7/1669 ,  F22B37/04 ,  F22B37/107 ,  F24H1/145 ,  F24H1/165 ,  F28D7/024 ,  F28F1/10 ,  F28F13/003 ,  Y10S165/401

    摘要： A heat transfer structure and system including a matrix of tubes and spheres bonded together to provide a conduit for a first fluid such as water and a plurality of interconnected paths for a second fluid such as hot flue gas. The paths are made up of the spaces between the spheres such that the walls of the paths are portions of spherical surfaces. The total path length is made less than twenty times the average radius of curvature of the spherical surfaces and the spacing between adjacent tube elements is of the same order of magnitude as the average length of the paths. A water heater or boiler so constructed may be made to transfer substantially all the heat in a flue gas to water in an average path length of one inch or less.

    摘要翻译： 传热结构和系统，其包括接合在一起的管和球体的矩阵，以提供用于第一流体（例如水）的导管和用于第二流体（例如热烟道气）的多个互连路径。 路径由球体之间的空间构成，使得路径的壁是球面的部分。 总路径长度小于球面的平均曲率半径的二十倍，并且相邻管元件之间的间隔与路径的平均长度具有相同的数量级。 可以制造如此构造的热水器或锅炉，以将烟道气中的大部分热量以一英寸或更小的平均路径长度传递给水。