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    • 1. 发明授权
    • Apparatus and method for treating geothermal steam which contains
hydrogen sulfide
    • 含硫化氢的地热蒸汽处理装置及方法
    • US4844162A
    • 1989-07-04
    • US139582
    • 1987-12-30
    • Brian W. MaassenRichard G. Campbell
    • Brian W. MaassenRichard G. Campbell
    • E21B41/00E21B43/40F03G7/04
    • F03G7/04E21B41/0057E21B43/40Y02E10/10Y10S423/19
    • Apparatus is provided for treating a flow of hot, pressurized, hydrogen sulfide-containing geothermal steam, particularly a flow of high-energy, surplus steam substantially as produced from the ground. The apparatus comprises a first condenser in which most of the steam in the flow is condensed, and a first separator in which the steam condensate is separated from residual amounts of steam and non-condensable gases (including hydrogen sulfide). An after-cooler is provided for cooling the condensate to a disposal temperature of less than about 200.degree. F. before the condensate is discharged into a disposal well, the disposal temperature being such as to create a vacuum in the disposal well. A second condenser is provided in which is condensed a substantial amount of the steam in the mixture of residual steam and non-condensable gases, the condensate being separated from a mixture of residual steam and non-condensable gases in a second separator. Condensate from the second separator is combined with condensate from the after-cooler and is discharged therewith into the disposal well. The mixture of non-condensable gases and residual amounts of steam is also discharged from the second separator into the disposal well, being drawn thereinto by the vacuum in the well. A corresponding method is provided for treating a flow of geothermal steam so as to control hydrogen sulfide emissions therefrom.
    • 提供了一种用于处理热,加压,含硫化氢的地热蒸汽的流动,特别是基本上从地面产生的高能量,多余的蒸汽流。 该装置包括第一冷凝器,其中流动中的大部分蒸汽被冷凝,以及第一分离器,其中蒸汽冷凝物与剩余量的蒸汽和不可冷凝气体(包括硫化氢)分离。 提供了后冷却器,用于在冷凝物排入处置井之前将冷凝物冷却至小于约200°F的处理温度,处置温度使得在处理井中产生真空。 提供了第二冷凝器,其中残余蒸汽和不可冷凝气体的混合物中的大量蒸汽冷凝,冷凝物与第二分离器中的残余蒸汽和不可冷凝气体的混合物分离。 来自第二分离器的冷凝物与来自后冷却器的冷凝物组合并且被排出到处理井中。 不可冷凝气体和残留量的蒸汽的混合物也从第二分离器排放到处理井中,并通过井中的真空吸入。 提供了一种相应的处理地热蒸汽流的方法,以控制其中的硫化氢排放。