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    • 29. 发明授权
    • Reduction of sulfur content in a gaseous stream
    • 减少气流中的硫含量
    • US5512260A
    • 1996-04-30
    • US205436
    • 1994-03-04
    • Thomas R. KilianyJohn P. McWilliamsDavid A. Pappal
    • Thomas R. KilianyJohn P. McWilliamsDavid A. Pappal
    • B01D53/86C01B17/04B01D53/48
    • B01D53/8615C01B17/0465
    • A process for reducing sulfur content in a gaseous stream with the production of elemental sulfur by first treating the gaseous steam with hydrogenation and hydrolysis to convert substantially all of the sulfur components therein to hydrogen sulfide. Then reducing the water content of the gaseous stream to optimize chemical equilibrium. Thereafter, the gaseous steam is contacted in an oxidation reactor with an acid catalyst at a temperature of about 150.degree. C. to about 350.degree. C. to convert hydrogen sulfide to elemental sulfur. The product gas leaving the oxidation reactor is cooled to separate elemental sulfur by condensation. The acid catalyst is a shape selective zeolite, a metal-exchanged or impregnated alumina, or a mixture thereof. The alumina is gamma phase alumina impregnated with from about 0.2 wt % to about 2.0 wt % metal.
    • 通过首先用氢化和水解处理气态蒸汽以将其中的所有硫成分基本上转化为硫化氢,从而降低产生元素硫的气流中的硫含量的方法。 然后减少气流的含水量以优化化学平衡。 此后,气态蒸汽在氧化反应器中与酸催化剂在约150℃至约350℃的温度下接触,以将硫化氢转化为元素硫。 离开氧化反应器的产物气体被冷却以通过冷凝分离元素硫。 酸催化剂是形状选择性沸石,金属交换或浸渍的氧化铝或其混合物。 氧化铝是用约0.2重量%至约2.0重量%金属浸渍的γ相氧化铝。