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Process for recovering as sulfur the compounds H2S, SO2, COS and/or CS2 in a tail gas from a sulfur plant

机译:从硫磺厂回收尾气中的H2S,SO2,COS和/或CS2化合物作为硫回收的方法

摘要

A process is provided to recover residual H2S, SO2, COS and CS2 in the tail gas from a sulphur recovery process. The tail gas is oxidized and hydrolyzed at a temperature of from 180° C. to 700° C. to provide an oxidized and hydrolyzed gas stream containing substantially no COS or CS2 and having a concentration by volume of H2S and SO2 such that the H2S concentration minus twice the SO2 concentration is from 0.25% to 0.5%. Then the gas stream from the hydrolysis is passed over a Claus catalyst, for example based on alumina and/or titanium oxide, for the reaction of H2S with SO2 to form sulphur and provide a gas stream with substantially no SO2. The resulting gas stream from the Claus reaction together with a gas containing free oxygen is then passed over an oxidation catalyst, such as one of more oxides or salts of Ni, Co, Fe, Cu, Ag, Mn, Mo, Cr, W or V, deposited on a support, such as bauxite, activated aluminia, silica, titanium oxide, zirconium oxide, zeolite or activated carbon to form sulphur and release a purified gas stream containing substantially no sulphur compounds.
机译:提供了一种从硫磺回收过程中回收尾气中残留的H 2 S,SO 2 ,COS和CS 2 的方法。尾气在180℃的温度下被氧化和水解。摄氏700度C.提供基本上不包含COS或CS 2 且浓度为H 2 S和SO 2 使得H 2 S浓度减去SO 2 浓度的两倍为0.25%至0.5%。然后将水解产生的气流通过例如基于氧化铝和/或二氧化钛的Claus催化剂,使H 2 S与SO 2 反应生成生成硫并提供基本不含SO 2 的气流。然后将来自克劳斯反应的所得气流与包含游离氧的气体一起流经氧化催化剂,例如Ni,Co,Fe,Cu,Ag,Mn,Mo,Cr,W或V,沉积在载体如铝土矿,活性铝,二氧化硅,氧化钛,氧化锆,沸石或活性炭上以形成硫并释放出基本上不含硫化合物的纯化气流。

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