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Efficiency of a Claus furnace in the coke-oven gas desulphurization circuit of MMK

机译:MMK焦炉气体脱硫电路中克劳斯炉的效率

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AbstractThe poor efficiency of the Claus furnace in sulfur removal at the coke plant of OAO Magnitogorskii Metallurgicheskii Kombinat (MMK) is analyzed on the basis of monitoring data for the sulfur recovery unit and thermodynamic calculations. The low level of sulfur removal from coke-oven gas (~60%) at OAO MMK is mainly due to thermodynamic limitations on the thermal stage of hydrogen-sulfide oxidation with the specific composition of the sour gas at coke plants: low hydrogen-sulfide concentration and combustion of the additional fuel (natural gas). With the kinetic constraints in the Claus furnace, the high CO2content in the sour gas (up to 37 vol %) results in increased yield of carbonyl sulfide (~14%). That calls for particular care in optimizing the temperature during the catalytic stages and selecting the best catalysts.]]>
机译:<![CDATA [<标题>抽象 ara>在OAO Magnitogorskii Metallurgicheskii Kombinat(MMK)的焦炭植物中硫磺除去的克劳斯炉中的效率较差,基于硫磺恢复的数据进行监测数据 单位和热力学计算。 OAO MMK的焦炉气体(〜60%)的低水平除去oa MMK的含水量主要是由于耐硫化氢氧化热阶段的热力学限制,在焦炭植物的酸气体的特定组合物中:低硫化氢 额外燃料(天然气)的浓度和燃烧。 通过克劳斯炉中的动力学约束,酸性气体中的高CO <下标> 2 含量(高达37体积%)导致羰基硫醚的产率增加(〜14%)。 该要求特别注意在催化阶段期间优化温度并选择最佳催化剂。]>

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