Process for treating a gas containing hydrogen sulphide and sulphur dioxide
    2.
    发明申请
    Process for treating a gas containing hydrogen sulphide and sulphur dioxide 有权
    用于处理含有硫化氢和二氧化硫的气体的方法

    公开(公告)号:US20060204433A1

    公开(公告)日:2006-09-14

    申请号:US11369821

    申请日:2006-03-08

    Abstract: A process for treating a gas containing hydrogen sulphide (H2S) and sulphur dioxide (SO2) is described in which: said gas is brought into contact at a suitable temperature with an organic solvent containing at least a soluble catalytic system, comprising at least one compound comprising at least one functional group A consisting of a carboxylic acid function and at least one functional group B comprising at least one nitrogen atom and which can produce an acid-base type reaction with at least one functional group A under the operating conditions of said process; a gaseous effluent substantially depleted in hydrogen sulphide and sulphur dioxide is recovered, along with liquid sulphur separated from the solvent by liquid-liquid decantation; said catalytic system which is employed slowing by-product formation.

    Abstract translation: 描述了一种处理含硫化氢(H 2 S 2 S)和二氧化硫(SO 2 H 2)的气体的方法,其中:所述气体在合适的温度下接触 含有至少一种可溶性催化体系的有机溶剂,其包含至少一种包含至少一种由羧酸官能团组成的官能团A和至少一种包含至少一个氮原子的官能团B的化合物,该官能团可以产生酸 - 在所述方法的操作条件下与至少一个官能团A的碱型反应; 回收基本上不含硫化氢和二氧化硫的气态流出液以及通过液 - 液倾析与溶剂分离的液态硫; 所述催化系统用于减缓副产物形成。

    Process for treating a gas containing hydrogen sulphide and sulphur dioxide
    5.
    发明授权
    Process for treating a gas containing hydrogen sulphide and sulphur dioxide 有权
    用于处理含有硫化氢和二氧化硫的气体的方法

    公开(公告)号:US07597872B2

    公开(公告)日:2009-10-06

    申请号:US11369821

    申请日:2006-03-08

    Abstract: A process for treating a gas containing hydrogen sulphide (H2S) and sulphur dioxide, contacting the gas at a suitable temperature with an organic solvent containing at least a soluble catalytic system, comprising at least one compound comprising at least one functional group A consisting of a carboxylic acid function and at least one functional group B comprising at least one nitrogen atom and which can produce an acid-base type reaction with at least one functional group A under the operating conditions of said process; and recovering a gaseous effluent substantially depleted in hydrogen sulphide and sulphur dioxide along with liquid sulphur separated from the solvent by liquid-liquid decantation.

    Abstract translation: 一种处理含有硫化氢(H 2 S)和二氧化硫的气体的方法,使气体在合适的温度下与含有至少一种可溶性催化体系的有机溶剂接触,所述有机溶剂包含至少一种包含至少一个由 羧酸官能团和至少一个含有至少一个氮原子的官能团B,其在所述方法的操作条件下可与至少一个官能团A产生酸碱型反应; 并回收基本上耗尽硫化氢和二氧化硫的气态流出物以及通过液 - 液倾析与溶剂分离的液态硫。

    Method of collecting mercaptans contained in a gaseous feed
    6.
    发明授权
    Method of collecting mercaptans contained in a gaseous feed 有权
    收集气态饲料中所含硫醇的方法

    公开(公告)号:US07192565B2

    公开(公告)日:2007-03-20

    申请号:US11194557

    申请日:2005-08-02

    CPC classification number: C10L3/10

    Abstract: The gaseous feed flowing in through line 1 is contacted in contacting zone ZA with a liquid solvent flowing in through line 2. The solvent comprises between 0.001% and 100% by weight of a liquid olefin. Contacting in zone ZA is carried out in the presence of an acid catalyst. The purified gaseous feed is discharged from zone ZA through line 3. The sulfide-laden solvent is discharged through line 4, then regenerated in unit RE. The regenerated solvent is recycled through lines 7 and 2 to zone ZA.

    Abstract translation: 通过管线1流动的气态进料在接触区ZA中与通过管线2流动的液体溶剂接触。溶剂包含0.001至100重量%的液体烯烃。 ZA区在酸催化剂存在下进行接触。 纯化的气体进料通过管线3从区域ZA排出。含硫化物的溶剂通过管线4排出,然后在单元RE中再生。 再生的溶剂通过管线7和2再循环到区域ZA。

    Method of collecting mercaptans contained in a gaseous feed
    8.
    发明申请
    Method of collecting mercaptans contained in a gaseous feed 有权
    收集气态饲料中所含硫醇的方法

    公开(公告)号:US20060034742A1

    公开(公告)日:2006-02-16

    申请号:US11194557

    申请日:2005-08-02

    CPC classification number: C10L3/10

    Abstract: The gaseous feed flowing in through line 1 is contacted in contacting zone ZA with a liquid solvent flowing in through line 2. The solvent comprises between 0.001% and 100% by weight of a liquid olefin. Contacting in zone ZA is carried out in the presence of an acid catalyst. The purified gaseous feed is discharged from zone ZA through line 3. The sulfide-laden solvent is discharged through line 4, then regenerated in unit RE. The regenerated solvent is recycled through lines 7 and 2 to zone ZA.

    Abstract translation: 通过管线1流动的气态进料在接触区ZA中与通过管线2流动的液体溶剂接触。 溶剂含有0.001%至100%重量的液态烯烃。 ZA区在酸催化剂存在下进行接触。 纯化的气态进料通过管线3从ZA区排出。 含硫化物的溶剂通过管线4排出,然后在单元RE中再生。 再生的溶剂通过管线7和2再循环到区域ZA。

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