Heat exchange apparatus and process
    1.
    发明授权
    Heat exchange apparatus and process 失效
    热交换装置和过程

    公开(公告)号:US5958364A

    公开(公告)日:1999-09-28

    申请号:US849023

    申请日:1997-05-27

    摘要: Heat exchange apparatus and process, particularly heat exchange primary reforming with the primary reformed gas being subjected to partial combustion (and optionally secondary reforming) and the resultant partially combusted gas being used as the heat exchange medium to supply heat required for the primary reforming. The apparatus includes process fluid inlet and outlet zones separated from the heat exchange zone by boundary means such as tube sheets or header pipes. A plurality of heat exchange tubes for a process fluid extending through a heat exchange zone from one of the boundary means and slideably engage at the other boundary means with seal tubes fastened to said other boundary means. The interior of the inner one of the seal tube and its associated heat exchange tube is provided with a constriction of reduced cross-sectional area forming a low pressure region downstream of said constriction, an expansion region of cross-sectional area greater than that of the constriction downstream of said constriction, and one or more passages through the wall of that inner tube connecting said low pressure region to the exterior of the inner tube. The passages are located within the overlapping region of the seal tube and heat exchange tube so as to provide a leakage flow path for heat exchange medium from the heat exchange zone through the overlapping region and said passages, into the low pressure region.

    摘要翻译: PCT No.PCT / GB96 / 01812 Sec。 371日期:1997年5月27日 102(e)日期1997年5月27日PCT提交1996年7月29日PCT公布。 公开号WO97 / 05947 日期1997年2月20日换热装置和方法,特别是与一次重整气体进行部分燃烧(和任选地二次重整)的热交换一次重整,并且所得到的部分燃烧气体用作热交换介质,以提供所需的热量 初级改革。 该装置包括通过诸如管板或集管的边界装置与热交换区分离的工艺流体入口和出口区域。 多个热交换管,用于从一个边界装置延伸穿过热交换区的工艺流体,并且在另一个边界装置处可滑动地与固定到所述另一个边界装置的密封管接合。 密封管及其相关联的热交换管的内部的内部设置有减小的横截面积的收缩部,形成在所述收缩部的下游的低压区域,横截面积的膨胀区域大于 在所述收缩部的下游收缩,以及穿过将所述低压区域连接到内管的外部的内管的壁的一个或多个通道。 通道位于密封管和热交换管的重叠区域内,从而将热交换介质的热交换介质通过重叠区域和所述通道提供到低压区域。