Process for the removal of HCN from gas mixtures
    21.
    发明授权
    Process for the removal of HCN from gas mixtures 失效
    从气体混合物中除去HCN的方法

    公开(公告)号:US5660807A

    公开(公告)日:1997-08-26

    申请号:US553588

    申请日:1996-05-13

    Abstract: The invention relates to a process for the removal of HCN from gas mixtures that contain at least HCN and sulfur compounds, especially from gas mixtures that are obtained by partial oxidation of hydrocarbons, by catalytic decomposition of HCN, as well as a catalyst for the decomposition of HCN. According to the invention, the gas mixture is brought into contact with a catalyst which decomposes the HCN by hydrogenation and/or by hydrolysis and COS that is contained in the gas mixture is decomposed at least partially in this catalyst by hydrolysis. Advantageously, a catalyst that is based on titanium oxide and/or zirconium oxide as a vehicle and that contains chromium oxide as an active component is used. Advantageously, the catalyst is reduced during catalyst production or before use with H.sub.2 and/or a reducing gas at temperatures above the operating temperature of catalytic decomposition.

    Abstract translation: PCT No.PCT / EP94 / 01646 Sec。 371日期:1996年5月13日 102(e)日期1996年5月13日PCT提交1994年5月20日PCT公布。 出版物WO94 / 29004 日期1994年12月22日本发明涉及从气体混合物中除去HCN的方法,所述气体混合物至少含有HCN和硫化合物,特别是通过烃的部分氧化获得的气体混合物,HCN的催化分解以及 用于分解HCN的催化剂。 根据本发明,使气体混合物与通过氢化和/或水解分解HCN的催化剂接触,并且气体混合物中包含的COS至少部分地通过水解在该催化剂中分解。 有利地,使用基于氧化钛和/或氧化锆作为载体并且含有氧化铬作为活性组分的催化剂。 有利地,催化剂在催化剂生产期间或在高于催化分解操作温度的温度下用H2和/或还原气体使用之前被还原。

    Process for the simultaneous removal of H.sub.2 S, SO.sub.2 and
elemental sulfur from gaseous mixtures
    22.
    发明授权
    Process for the simultaneous removal of H.sub.2 S, SO.sub.2 and elemental sulfur from gaseous mixtures 失效
    同时从气体混合物中除去H 2 S,SO 2和元素硫的方法

    公开(公告)号:US4530827A

    公开(公告)日:1985-07-23

    申请号:US545427

    申请日:1983-10-26

    CPC classification number: B01D53/523 C01B17/05 C10K1/16

    Abstract: A process for the simultaneous removal of H.sub.2 S, SO.sub.2 and elemental sulfur from gaseous mixtures, comprises treating the gaseous mixture with a solvent. After the solvent becomes loaded with the components to be removed, it is regenerated and reused. In order to obtain savings in costs and energy, the sulfur is separated from the loaded solvent by lowering the temperature thereof. In this way, chemical regeneration of the scrubbing medium takes place within the cycle eliminating the requirement for outside regenerating apparatus.

    Abstract translation: 从气体混合物中同时除去H 2 S,SO 2和元素硫的方法包括用溶剂处理气态混合物。 溶剂加载待除去的组分后,再次再生再利用。 为了节省成本和能量,通过降低其温度将硫与负载的溶剂分离。 以这种方式,洗涤介质的化学再生在循环内进行,消除了对外部再生装置的要求。

    Recycle of hydrogenated sulfur plant tail gas to sour gas scrubbing
system
    23.
    发明授权
    Recycle of hydrogenated sulfur plant tail gas to sour gas scrubbing system 失效
    氢化硫厂尾气回收到酸性气体洗涤系统

    公开(公告)号:US4425317A

    公开(公告)日:1984-01-10

    申请号:US328554

    申请日:1981-12-08

    CPC classification number: B01D53/1462 C01B17/0456 Y02C10/06 Y02P20/152

    Abstract: In a process for the separation of at least carbon dioxide and hydrogen sulfide from a raw gaseous mixture to form a purified gaseous mixture comprising passing said gas through a sour gas removal system including the steps of scrubbing said gaseous mixture with a liquid scrubbing agent having a higher affinity for hydrogen sulfide than for carbon dioxide, removing from said system an off-gas enriched in hydrogen sulfide, and passing said off-gas to a sulfur recovery system comprising the conversion of sulfur values to elemental sulfur and the recovery of a tail gas containing hydrogen sulfide and sulfur dioxide,the improvement which comprises hydrogenating said tail gas to convert sulfur dioxide to hydrogen sulfide and recycling resultant hydrogenated tail gas to said sour gas removal system, whereby essentially no hydrogen sulfide or sulfur dioxide is discharged into the environment.

    Abstract translation: 在用于从原始气体混合物中分离至少二氧化碳和硫化氢以形成纯化的气体混合物的方法中,包括使所述气体通过酸性气体去除系统,所述气体混合物包括用液体洗涤剂洗涤所述气体混合物的步骤,所述液体洗涤剂具有 对硫化氢的亲合力高于二氧化碳,从所述系统中除去富含硫化氢的废气,并将所述废气送至硫回收系统,硫回收系统包括将硫值转化为元素硫并回收尾气 含有硫化氢和二氧化硫的改进包括使所述尾气氢化以将二氧化硫转化为硫化氢,并将所得氢化尾气再循环到所述酸性气体去除系统,由此基本上不将硫化氢或二氧化硫排放到环境中。

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