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    • 1. 发明授权
    • Steam condensing apparatus with freeze-protected vent condenser
    • 具有防冻通风冷凝器的蒸汽冷凝设备
    • US5765629A
    • 1998-06-16
    • US585342
    • 1996-04-10
    • James David GoldsmithGeorge Edward KluppelGeorge Steve MillasThomas Wayne Strock
    • James David GoldsmithGeorge Edward KluppelGeorge Steve MillasThomas Wayne Strock
    • F28B1/06F28B9/08F28B9/10
    • F28B9/08F28B1/06F28B9/10F28B2001/065Y10S165/913
    • A two-stage steam condenser that prevents freezing from occurring in the tube rows by continual purging of the tube rows. Such continual purging prevents any steam from back-flowing into a tube row thereby eliminating the possibility that condensate or noncondensable gases will become trapped therein. This is achieved by isolating each of the tube rows in the second stage of the condenser so that the pressure of one tube row is not exposed to the pressure occurring in another adjacent tube row. The condensate collected in the various tube rows of this second stage is delivered to a common drain pot that is hydraulically balanced to accommodate the various pressures in these tube rows. Such hydraulic balancing also prevents any back-flowing from occurring from one tube row into another. Furthermore, in this second stage of the steam condenser, the steam and resulting condensate both flow concurrently downward while any noncondensable gases are vented counter-currently upward against such steam and condensate flow.
    • 两级蒸汽冷凝器,通过连续吹扫管排,防止管排中发生冻结。 这种持续吹扫防止任何蒸汽回流到管排中,从而消除了冷凝物或不可冷凝气体将被捕获在其中的可能性。 这通过隔离冷凝器的第二级中的每个管排来实现,使得一个管排的压力不暴露于在另一相邻管排中发生的压力。 收集在该第二阶段的各管排中的冷凝物被输送到液压平衡以容纳这些管排中的各种压力的公共排水罐。 这种液压平衡还防止从一个管排发生到另一个管排的任何反向流动。 此外,在蒸汽冷凝器的第二阶段中,蒸汽和产生的冷凝物两者同时向下流动,而任何不可冷凝气体相对于这种蒸汽和冷凝物流反向排出。
    • 3. 发明授权
    • Apparatus for air sparged slurry tanks
    • 鼓风泥浆罐装置
    • US6013120A
    • 2000-01-11
    • US702425
    • 1996-08-14
    • Wadie Fawzy GoharaThomas Wayne StrockJohn Ronald Cline
    • Wadie Fawzy GoharaThomas Wayne StrockJohn Ronald Cline
    • B01F3/04B01F3/08
    • B01F3/0876B01F3/04262B01F3/04468B01F2003/04148B01F2003/04319B01F2003/04326B01F2003/04361B01F3/04099Y10S261/09
    • A device for using the density control water to continuously flush the oxidation air header and the sparge pipes in a flue gas wet scrubber agitation tank. The density control line is routed to the elevation where the control valve is located. A U-shaped trap is located between the control valve and air sparge header such that the density control water joins the humidified oxidation air. A liquid layer forms on the floor of the header and is moved toward the distant side of the header by the motion of the air passing on top of the liquid layer and by the continuous flow of water. The bottom section of the main header is perforated to allow the flowing water to exit the header into the tank and flush any accumulated solids that might penetrate the header through the air holes. The air holes are located in a section at a minimum of five degrees off the floor and maximum of one hundred eighty degrees off the header bottom and preferably at forty-five degrees. The distant end of the header has an opening located close to the header floor to provide an outlet for the flushed solids and prevents the formation of back waves in the header.
    • 一种使用密度控制水连续冲洗氧化空气集管和烟道气体湿式洗涤器搅拌槽中的喷射管的装置。 密度控制线路线到控制阀所在的高度。 U形捕集器位于控制阀和空气喷射头之间,使得密度控制水与加湿的氧化空气结合。 液体层形成在集管的地板上,并且通过在液体层顶部的空气的运动以及连续的水流而移动到集管的远侧。 主集管的底部是穿孔的,以使流动的水从集管中排出到容器中,并冲洗可能通过气孔穿过集管的任何积聚的固体。 气孔位于距离地板最少五度的区域中,最大距离底部最大一百八十度,最好为四十五度。 集管的远端具有靠近集管底板的开口,以为冲洗的固体提供出口,并防止在集管中形成反向波。
    • 4. 发明授权
    • Method and apparatus for air sparged slurry tanks
    • 鼓风泥浆罐的方法和装置
    • US6086658A
    • 2000-07-11
    • US366844
    • 1999-08-04
    • Wadie Fawzy GoharaThomas Wayne StrockJohn Ronald Cline
    • Wadie Fawzy GoharaThomas Wayne StrockJohn Ronald Cline
    • B01F3/04B01F3/08
    • B01F3/0876B01F3/04262B01F3/04468B01F2003/04148B01F2003/04319B01F2003/04326B01F2003/04361B01F3/04099Y10S261/09
    • A method and device for using the density control water to continuously flush the oxidation air header and the sparge pipes in a flue gas wet scrubber agitation tank. The density control line is routed to the elevation where the control valve is located. A U-shaped trap is located between the control valve and air sparge header such that the density control water joins the humidified oxidation air. A liquid layer forms on the floor of the header and is moved toward the distant side of the header by the motion of the air passing on top of the liquid layer and by the continuous flow of water. The bottom section of the main header is perforated to allow the flowing water to exit the header into the tank and flush any accumulated solids that might penetrate the header through the air holes. The air holes are located in a section at a minimum of five degrees off the floor and maximum of one hundred eighty degrees off the header bottom and preferably at forty-five degrees. The distant end of the header has an opening located close to the header floor to provide an outlet for the flushed solids and prevents the formation of back waves in the header.
    • 一种使用密度控制水连续冲洗氧化空气集管和烟道气体湿式洗涤器搅拌槽中的喷射管的方法和装置。 密度控制线路线到控制阀所在的高度。 U形捕集器位于控制阀和空气喷射头之间,使得密度控制水与加湿的氧化空气结合。 液体层形成在集管的地板上,并且通过在液体层顶部的空气的运动以及连续的水流而移动到集管的远侧。 主集管的底部是穿孔的,以使流动的水从集管中排出到容器中,并冲洗可能通过气孔穿过集管的任何积聚的固体。 气孔位于距离地板最少五度的区域中,最大距离底部最远一百八十度,最好四十五度。 集管的远端具有靠近集管底板的开口,以为冲洗的固体提供出口,并防止在集管中形成反向波。