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    • 3. 发明授权
    • Air conditioner heat-exchanger
    • 空调热交换器
    • US5975198A
    • 1999-11-02
    • US976724
    • 1997-11-24
    • Young-Saeng KimBaek Youn
    • Young-Saeng KimBaek Youn
    • F28F1/32F28D1/04
    • F28F1/32Y10S165/501Y10S165/91
    • An air conditioner heat-exchanger is provided to smoothen the air flowing through a plurality of the heat transfer tubes, thereby improving heat transference efficiency and heat-exchange effect, the air conditioner heat-exchanger having a plurality of flat fins arranged in parallel at a predetermined interval and a plurality of heat transfer tubes perpendicularly inserted to the plurality of flat fins, the plurality of heat transfer tubes being arranged against the air flowing direction (S) with a predetermined horizontal interval (X) and a predetermined vertical interval (Y) maintained therebetween to avoid the influence of the dead air region (P) formed therebehind.
    • 提供一种空调热交换器,用于使流过多个传热管的空气平滑,从而提高热传递效率和热交换效果,空调热交换器具有多个平行翅片,平行于 所述多个传热管以预定的水平间隔(X)和预定的垂直间隔(Y)相对于所述空气流动方向(S)布置,所述多个传热管垂直地插入所述多个扁平翅片, 保持在它们之间以避免在其上形成的死空气区域(P)的影响。
    • 4. 发明授权
    • Cross-flow, fixed-bed catalytic reactor
    • 交叉流动,固定床催化反应器
    • US5520891A
    • 1996-05-28
    • US189968
    • 1994-02-01
    • Jing M. Lee
    • Jing M. Lee
    • B01J8/02F28D7/08C07C31/04
    • B01J8/0285B01J8/025F28D7/08F28D7/085B01J2208/00141B01J2219/00083F28F2275/02Y10S165/91Y10S423/12
    • Disclosed are a fixed-bed, cross-flow catalytic reactor wherein reaction heat can be exchanged against a heat exchange medium circulating indirectly through the catalyst bed, and a catalytic process comprising operation of the cross-flow reactor. The reactor comprises a catalyst bed having internally embedded banks of heat exchange tubes. An inlet distributor distributes reactants along the axial length of the bed. The distributed fluid passes through the bed in a cross-flow path wherein a catalytic reaction occurs. The reaction effluent is then collected from the bed by an outlet product collector. A heat exchange medium circulated through the internal heat exchange tubes adds or removes reaction heat as required for enhanced conversion in the reactor. Multiple heat exchange tubes can be used, and inlet and discharge manifolds are provided for distributing the circulating heat exchange medium. The heat exchange tubes can be spaced in accordance with the heat interchange required to optimize the reaction rate. A relatively shorter cross-flow path through a relatively larger flow area enhances reactor performance by allowing the catalyst particle size to be reduced without substantially increasing pressure drop.
    • 公开了一种固定床交叉催化反应器,其中反应热可以间接地通过催化剂床循环的热交换介质和包括流动反应器的操作的催化方法交换。 反应器包括具有内部嵌入的热交换管组的催化剂床。 入口分配器沿着床的轴向长度分布反应物。 分布的流体在其中发生催化反应的交叉流动路径中通过床。 然后通过出口产物收集器从床中收集反应流出物。 循环通过内部热交换管的热交换介质根据反应器中提高的转化所需加入或除去反应热。 可以使用多个换热管,并且提供入口和排出歧管以分配循环热交换介质。 热交换管可以根据优化反应速率所需的热交换间隔开。 通过相对较大的流动面积的相对较短的横流路径通过允许催化剂粒度减小而基本上不增加压降来提高反应器性能。
    • 5. 发明授权
    • Finned-duct heat exchanger
    • 翅片管换热器
    • US5318112A
    • 1994-06-07
    • US25146
    • 1993-03-02
    • Stanislav Gopin
    • Stanislav Gopin
    • F28D1/053F28F1/28F28F1/32F28F13/12F28D1/04F28F1/02F28F1/18
    • F28D1/05366F28D1/05383F28F1/28F28F1/325F28F13/12Y10S165/91
    • A finned heat exchanger for increased heat transfer from liquid to air, includes of a plurality of stacked thin plates of conductive metal sheeting which are provided with stamped and drawn, slightly conical collars of elliptical, oval or other oblong cross section. The plates are stacked and assembled with the collars of each sheet forcefully pushed into the collars of the adjoining plate, thus effecting tightly closed ducts for the passage of the liquid. The thus-created ducts are arranged in rows and columns, wherein the long axes of the oblong cross section are inclined towards the center line of each column at an angle of 12.degree.-16.degree. to the left and to the right in alternate columns, and wherein the ducts in the rows are staggered in the direction of air flow, every second duct being disposed in forward direction by about half the length of the long axis of its cross section.
    • 一种用于增加从液体传播到空气的翅片式热交换器,包括多个层叠的导电金属片的薄板,其具有椭圆形,椭圆形或其它长方形横截面的冲压和拉伸的略微锥形的环形。 这些板被堆叠并组装,每个片的轴环被强制地推入毗邻板的套环中,从而实现紧密封闭的管道以使液体通过。 这样制造的管道以行和列布置,其中长方形横截面的长轴在每列的中心线以相对于左列和右侧的12°-16°的角度倾斜, 并且其中行中的管道在空气流动的方向上交错,每第二管道沿着其横截面的长轴的长度方向向前方向设置。
    • 6. 发明授权
    • Heat exchanger having improved tube layout
    • 热交换器具有改进的管布局
    • US5277247A
    • 1994-01-11
    • US905452
    • 1992-06-29
    • Gordon M. Cameron
    • Gordon M. Cameron
    • B01D1/06C01B17/80F28D7/16F28F9/22F28D7/10
    • F28D7/163B01D1/06C01B17/806F28F9/22Y10S165/91
    • A heat exchanger for exchanging heat between fluids comprising a shell and five tube bundles laid out as to collectively form a series of concentric pentagons, wherein each adjacent pair of tube bundles define an angle of 108.degree. and extend longitudinally within said shell and define a central space between them, said central space also extending longitudinally in said shell and being parallel to said tubes; each tube bundle consisting of a plurality of longitudinally extending parallel tubes in end view laid out in a set of parallel lines wherein each tube on a first parallel line with the two nearest tubes each on a second line adjacent to said first line forms an isosceles triangle having one angle of 72.degree. and two angles each of 54.degree.. This allows simple heat exchanger tube layout which is easy to fabricate and provide a compact tube bundle. The tube layout utilizes core tube entry of fluids and can accommodate internal core tubes or bypasses to cope with differential expansion.
    • 一种热交换器,用于在流体之间交换热量,所述热交换器包括外壳和布置成共同形成一系列同心五边形的五个管束,其中每个相邻的一对管束限定108度的角度并且在所述壳体内纵向延伸并限定中心 所述中心空间也在所述外壳中纵向延伸并平行于所述管; 每个管束由端部视图中的多个纵向延伸的平行管组成,其平行管线布置在一组平行线中,其中在与第一线相邻的第二线上的两个最近的管的第一平行线上的每个管形成等腰三角形 具有72度的一个角度和54度的两个角度。 这允许简单的热交换器管布置,其易于制造并且提供紧凑的管束。 管道布局利用流体的芯管进入,并且可以容纳内部核心管或旁路以应对差动膨胀。
    • 7. 发明授权
    • Heat exchanger
    • 热交换器
    • US4800955A
    • 1989-01-31
    • US106237
    • 1987-10-08
    • Klaus HagemeisterAlfred Hueber
    • Klaus HagemeisterAlfred Hueber
    • F28D1/047F28D7/06
    • F28D7/06Y10S165/436Y10S165/91
    • A heat exchanger having an inlet duct for admission of a first fluid to be heated, an outlet duct for discharge of the first fluid after heating thereof, the ducts being arranged in substantially parallel relation, and an assembly of a plurality of heat exchanger tubes connected to the inlet and outlet ducts for receiving the first fluid from the inlet duct to convey the first fluid through the tubes for discharge into the outlet duct. The heat exchanger tubes are of U-shape, each including first and second straight leg portions respectively connected to the inlet and outlet ducts and a curved bend region connecting the straight leg portions for reversing the direction of flow of the first fluid from the first leg portion to the second leg portion. The assembly of heat exchanger tubes projects laterally of the ducts into the path of travel of a second fluid which flows around the tubes in a passage area. The heat exchanger tubes are arranged in a matrix of rows and columns in which the straight leg portions of the tubes are spaced apart a greater distance than the spacing between the curved bend regions of the tubes.
    • 一种热交换器,其具有用于容纳待加热的第一流体的入口管道,用于在加热之后排放第一流体的出口管道,所述管道基本上平行地布置,并且连接多个热交换器管道的组件 到入口管道和出口管道,用于从入口管道接收第一流体,以将第一流体输送通过管子以排放到出口管道中。 热交换器管是U形的,每个包括分别连接到入口和出口管道的第一和第二直脚部分和连接直腿部分的弯曲弯曲区域,用于反转第一流体从第一腿部流动的方向 部分到第二腿部。 热交换器管的组件将管道的横向突出到在通道区域中围绕管流动的第二流体的行进路径。 热交换器管布置成行和列的矩阵,其中管的直脚部分间隔开比管的弯曲弯曲区域之间的间隔更大的距离。