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    • 3. 发明授权
    • Reactor, and method for the production of hydrogen sulfide
    • 反应器和生产硫化氢的方法
    • US08021624B2
    • 2011-09-20
    • US12523180
    • 2008-01-14
    • Andreas WölfertHerald JachowHeinz Drieβ
    • Andreas WölfertHerald JachowHeinz Drieβ
    • B01J8/44C01B17/00C01B17/33
    • C01B17/162B01J8/008B01J8/067B01J10/005B01J19/0053B01J19/242
    • The invention relates to a reactor (1) and a process for continuously preparing H2S by converting a reactant mixture which comprises essentially gaseous sulfur and hydrogen over a catalyst, comprising a sulfur melt (9) at least in a lower subregion (8) of the reactor (1), into which gaseous hydrogen is introduced. The catalyst is arranged in at least one U-shaped tube (21) which is partly in contact with the sulfur melt (9), the at least one U-shaped tube (21) having at least one entry orifice (23) on a limb (26) above the sulfur melt (9), through which the reactant mixture can enter the U-shaped tube (21) from a reactant region (10) of the reactor (1), having a flow path within the at least one U-shaped tube, along which the reactant mixture can be converted in a reaction region comprising the catalyst (22), and having at least one exit orifice (24) in another limb (27) through which a product can exit into a product region (7).
    • 本发明涉及一种反应器(1)和通过将包含基本上气态的硫和氢的反应物混合物转化成催化剂来连续制备H 2 S的方法,所述催化剂包含至少在下部(8)中的硫熔体(9) 反应器(1),其中引入气态氢。 该催化剂被布置在至少一个与硫熔体(9)接触的U形管(21)中,该至少一个U形管(21)具有至少一个入口孔(23) 所述硫磺熔体(9)上方的所述四肢(26),所述反应物混合物可从所述反应物区域(10)从所述反应物区域(10)进入所述U形管(21),所述反应物区域(10)具有在所述至少一个 U形管,反应物混合物沿着该反应物混合物可以在包含催化剂(22)的反应区域中转化,并且在另一个分支(27)中具有至少一个出口孔(24),产品可以通过该出口孔排出到产品区域 (7)。
    • 4. 发明授权
    • Method and device for continuous production of hydrogen sulphide
    • 连续生产硫化氢的方法和装置
    • US07887777B2
    • 2011-02-15
    • US12523346
    • 2008-01-15
    • Andreas WölfertHerald JachowHeinz Drieβ
    • Andreas WölfertHerald JachowHeinz Drieβ
    • B01J19/00C01B17/16
    • C01B17/168C01B17/162
    • Hydrogen sulfide H2S is prepared from a crude gas stream containing H2S and polysulfanes (H2Sx). The crude gas stream is passed at temperatures of from 114 to 165° C. through catalytically active material present in a vessel, and sulfur is collected in the bottom of the vessel and recycled to the preparation of H2S. This process may be accomplished in an apparatus including a reactor for reacting sulfur and hydrogen, a cooler for receiving and cooling an H2S-containing crude gas stream passed out of the reactor to between 114 to 165° C., a vessel coupled to the cooler, the vessel including catalytically active material and a bottom for collecting sulfur obtained from the crude gas stream, and a line which is connected to the bottom of the vessel and opens into the cooler or into the reactor, for recycling sulfur.
    • 硫化氢H2S由含H2S和聚硫烷(H2Sx)的粗气流制备。 粗气流在114至165℃的温度下通过存在于容器中的催化活性材料,并将硫收集在容器的底部并再循环至制备H 2 S。 该方法可以在包括用于使硫和氢反应的反应器的装置中实现,冷却器用于接收和冷却从反应器排出的含H2S的粗气流至114至165℃,与冷却器连接的容器 该容器包括催化活性材料和用于收集从粗气流获得的硫的底部,以及连接到容器底部并且通向冷却器或反应器中的用于再循环硫的管线。