Process for the removal of s02, hcn and h2s and optionally cos, cs2 and nh3 from a gas stream
    1.
    发明申请
    Process for the removal of s02, hcn and h2s and optionally cos, cs2 and nh3 from a gas stream 失效
    从气流中去除s02,hcn和h2s以及任选的cos,cs2和nh3的方法

    公开(公告)号:US20060272502A1

    公开(公告)日:2006-12-07

    申请号:US10558448

    申请日:2004-05-28

    Abstract: The invention relates to a process for the removal of SO2, HCN and H2S and optionally one or more compounds from the group of COS, CS2 and NH3 from a first gas stream, which process comprises the steps of: (a) removing SO2 from the first gas stream by contacting the first gas stream in a hydrogenation zone with a hydrogenation catalyst in the presence of hydrogen to obtain a second gas stream; (b) removing HCN and optionally COS and/or CS2 from the second gas stream obtained in step (a) by contacting the second gas stream in a hydrolysis zone with a hydrolysis catalyst in the presence of water to obtain a third gas stream; (c) removing NH3 from the third gas stream by contacting the third gas stream in a NH3-removal zone with an aqueous acidic washing liquid to obtain an ammonium-comprising aqueous stream and a fourth gas stream; (d) removing H2S from the fourth gas stream by contacting the fourth gas stream in a H2S-removal zone with an aqueous alkaline washing liquid to obtain a H2S-depleted gas stream and a hydrogensulphide-comprising aqueous stream; (e) contacting the hydrogensulphide-comprising aqueous stream obtained in step (d) with sulphide-oxidizing bacteria in the presence of oxygen in an oxidation reactor to obtain a sulphur slurry and a regenerated aqueous alkaline washing liquid; (f) separating at least part of the sulphur slurry obtained in step (e) from the regenerated aqueous alkaline washing liquid and; (g) recycling regenerated aqueous alkaline washing liquid obtained in step (e) to the H2S-removal zone in step (d).

    Abstract translation: 本发明涉及一种除去SO 2 H 2,HCN和H 2 S以及任选的一种或多种COS,CS 2, / SUB和NH 3,该方法包括以下步骤:(a)通过使第一气流与第一气流接触除去SO 2, 在氢化催化剂的氢化区中,在氢的存在下,得到第二气流; (b)通过在水存在下使水解区中的第二气流与水解催化剂接触,从步骤(a)中获得的第二气流中除去HCN和任选的COS和/或CS 2 以获得第三气流; (c)通过使NH 3 - 去除区域中的第三气流与酸性洗涤液接触,从第三气流中除去NH 3,得到含铵的 水流和第四气流; (d)通过使H 2 S 2去除区中的第四气流与碱性洗涤液接触,从第四气流中除去H 2 S,得到H S 2贫的气流和含硫化氢的水流; (e)在氧化反应器中将氧化反应器中的步骤(d)中获得的含硫化氢的水流与硫氧化物 - 氧化细菌接触以获得硫浆料和再生碱性碱性洗涤液; (f)将步骤(e)中获得的硫浆料的至少一部分与再生碱性碱性洗涤液分离; (g)在步骤(d)中将步骤(e)中获得的再生水性碱性洗涤液再循环到H 2 S去除区。

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