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Process for modifying the sulphur yield of a plant producing sulphur from an acid gas containing hydrogen sulphide, whereby a sulphur production plant is followed by a purification unit

机译:改变由含硫化氢的酸性气体生产硫的工厂的硫收率的方法,其中硫生产工厂之后是提纯单元

摘要

The sulphur plant (1), in which the acid gas (8) and a gas containing free oxygen (9) are introduced, produces sulphur by controlled oxidation of the H2S in the acid gas and also supplies the residual gas (17b) containing H2O, H2S, SO2 and at least one of the derivatives COS and CS2. Said residual gas is contacted with a catalytic (2) for hydrolysing the COS and CS2 derivatives into H2S operating between 180 DEG C and 400 DEG C in order to produce a hydrolysed residual gas containing H2S and SO2 and essentially free from COS and CS2. The hydrolysed residual gas (38) is introduced into a purification unit (3) into which are fed H2S and SO2 in order to be reacted to form sulphur, by operating at a temperature below the dew point of the sulphur formed and to obtain in addition, as an output (29) of said unit, a purified residual gas which is then incinerated (4). The H2S resulting from the hydrolysis of COS and CS2 is almost entirely recovered in the form of sulphur in the purification unit, which enables an improved sulphur output of the overall installation.
机译:引入了酸性气体(8)和含游离氧的气体(9)的硫磺装置(1)通过控制酸性气体中的H2S氧化产生硫磺,并还提供含H2O的残余气体(17b) ,H 2 S,SO 2和衍生物COS和CS2中的至少一种。所述残留气体与催化剂(2)接触,以将COS和CS2衍生物水解成在180℃至400℃之间操作的H2S,以产生包含H2S和SO2且基本上不含COS和CS2的水解残留气体。通过在低于所形成的硫的露点的温度下进行操作,将水解后的残余​​气体(38)引入纯化单元(3)中,向其中加入H2S和SO2以使其反应生成硫。作为所述单元的输出(29),然后将纯化的残余气体焚化(4)。 COS和CS2水解产生的H2S在纯化单元中几乎全部以硫的形式回收,这可以提高整个设备的硫输出。

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