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    • 4. 发明授权
    • Interface fluid heat transfer system
    • 界面流体传热系统
    • US4911233A
    • 1990-03-27
    • US234582
    • 1988-08-22
    • James C. ChaoTzer-Fen Chen
    • James C. ChaoTzer-Fen Chen
    • B01D5/00F28B3/02
    • B01D5/0027F28B3/02Y10S165/162Y10S165/907Y10S165/913
    • A process for condensing vapor or mist material onto a thin first liquid film surface, which liquid film is generated and supported on the outer surface of a porous structure. A moving condensable vapor contacts the thin liquid film and is condensed onto the liquid surface. The condensed vapor drains by gravity action into a collection zone, together with a portion of the liquid film material being entrained therein. The vapor or mist material can be either substantially immiscible or miscible in the liquid film. The first liquid is preferably provided in a closed system and is recycled at near ambient temperature and at pressure conditions sufficient to produce the thin liquid film external to the porous structure, which has a porosity of 20-80%. An apparatus including the porous structure and liquid handling system for condensing an upflowing condensable vapor is disclosed.
    • 一种用于将蒸气或雾材料冷凝到薄的第一液膜表面上的方法,该薄膜在多孔结构的外表面上产生和支撑。 移动的可冷凝蒸汽接触薄液膜并冷凝到液体表面上。 冷凝的蒸汽通过重力作用排入收集区,一部分液膜材料被夹带在其中。 蒸气或烟雾材料可以与液膜基本上是不混溶的或可混溶的。 第一液体优选地设置在封闭系统中,并且在接近环境温度和足以产生孔隙率为20-80%的多孔结构外部的薄液体膜的压力条件下再循环。 公开了一种包括用于冷凝可向上流动的可冷凝蒸气的多孔结构和液体处理系统的装置。
    • 9. 发明授权
    • Distributor for a flowable medium
    • 可流动介质的分配器
    • US08291968B2
    • 2012-10-23
    • US12063437
    • 2006-08-09
    • Gregory Mark Paxton
    • Gregory Mark Paxton
    • F28B3/02
    • B01D3/008B01D1/065B01J19/0053B01J2219/00247F28D3/04
    • A distributor of flowable medium for a heat exchanger has a housing member and at least one substantially vertically oriented tube member arranged therein. The distributor has a hollow body arranged to be supported in one end of the tube member. An upturned funnel shaped core member is formed in the hollow body, resulting in an annular flow passage between the body and the core member. The body has an upper section with an inlet, a lower section with an outlet, and a mid section between the upper and lower sections. The flow passage extends from the inlet to the outlet at the lower section, and is configured to narrow progressively from the inlet towards the mid section, and widen progressively from the mid section towards the outlet for modifying flow characteristics of the medium flowing through the passage. Intake guide elements are provided at the upper section.
    • 用于热交换器的可流动介质的分配器具有壳体构件和布置在其中的至少一个基本垂直定向的管构件。 分配器具有中空体,其布置成被支撑在管构件的一端中。 在中空体中形成有向上的漏斗形的芯部件,从而在主体和芯部件之间产生环形的流动通道。 主体具有上部,其具有入口,下部具有出口,以及在上部和下部之间的中间部分。 流动通道在下部从入口延伸到出口,并且构造成从入口朝向中间部分逐渐缩小,并且逐渐从中间部分朝向出口扩宽,以改变流过通道的介质的流动特性 。 进气导向元件位于上部。
    • 10. 发明授权
    • Method and apparatus for high-efficiency direct contact condensation
    • 高效直接接触冷凝的方法和装置
    • US5925291A
    • 1999-07-20
    • US824236
    • 1997-03-25
    • Desikan BharathanYves ParentA. Vahab Hassani
    • Desikan BharathanYves ParentA. Vahab Hassani
    • F28B3/00B01J19/00F28B3/02F28B3/04F28C1/00F28F25/06F28F25/08B01F3/04
    • F28F25/087F28B3/02F28B3/04F28F25/06Y10S261/10Y10S261/32
    • A direct contact condenser having a downward vapor flow chamber and an upward vapor flow chamber, wherein each of the vapor flow chambers includes a plurality of cooling liquid supplying pipes and a vapor-liquid contact medium disposed thereunder to facilitate contact and direct heat exchange between the vapor and cooling liquid. The contact medium includes a plurality of sheets arranged to form vertical interleaved channels or passageways for the vapor and cooling liquid streams. The upward vapor flow chamber also includes a second set of cooling liquid supplying pipes disposed beneath the vapor-liquid contact medium which operate intermittently in response to a pressure differential within the upward vapor flow chamber. The condenser further includes separate wells for collecting condensate and cooling liquid from each of the vapor flow chambers. In alternate embodiments, the condenser includes a cross-current flow chamber and an upward flow chamber, a plurality of upward flow chambers, or a single upward flow chamber. The method of use of the direct contact condenser of this invention includes passing a vapor stream sequentially through the downward and upward vapor flow chambers, where the vapor is condensed as a result of heat exchange with the cooling liquid in the contact medium. The concentration of noncondensable gases in the resulting condensate-liquid mixtures can be minimized by controlling the partial pressure of the vapor, which depends in part upon the geometry of the vapor-liquid contact medium. In another aspect of this invention, the physical and chemical performance of a direct contact condenser can be predicted based on the vapor and coolant compositions, the condensation conditions. and the geometric properties of the contact medium.
    • 具有向下蒸汽流动室和向上蒸气流动室的直接接触冷凝器,其中每个蒸汽流室包括多个冷却液供应管和布置在其下的气液接触介质,以便于接触和直接热交换 蒸汽和冷却液体。 接触介质包括布置成形成用于蒸气和冷却液体流的垂直交错通道或通道的多个片材。 向上蒸气流动室还包括设置在蒸汽 - 液体接触介质下方的第二组冷却液供应管,其响应于向上蒸气流动室内的压差而间歇地操作。 冷凝器还包括用于从每个蒸汽流室收集冷凝物和冷却液体的单独的井。 在替代实施例中,冷凝器包括交流流动室和向上流动室,多个向上流动室或单个向上流动室。 使用本发明的直接接触式冷凝器的方法包括使蒸气流顺序地通过向下和向上的蒸气流室,其中由于与接触介质中的冷却液体的热交换而使蒸汽冷凝。 可以通过控制部分地取决于气液接触介质的几何形状的蒸气的分压来使得到的冷凝液 - 液体混合物中的不可冷凝气体的浓度最小化。 在本发明的另一方面,可以基于蒸汽和冷却剂组合物,冷凝条件来预测直接接触冷凝器的物理和化学性能。 和接触介质的几何性质。