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Method for refining coke oven gas in wet desulfurizing process
Method for refining coke oven gas in wet desulfurizing process
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机译:湿法脱硫炼焦炉煤气的精制方法
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摘要
PURPOSE: A method for optimizing reaction in which high toxic sodium cyanide is changed into harmless sodium thiocyanate by sulfur by pre-calculating content of sulfur required for removing cyan that is an impurity of coke oven gas and properly maintaining content of sulfur in wet desulfurizing process is provided. CONSTITUTION: The method for refining coke oven gas in wet desulfurizing process comprises first step of supplying coke oven gas and sodium hydroxide (NaOH) into an absorption column(10), producing sodium hydrogen sulfide (NaHS) and sodium cyanide (NaCN) by reacting hydrogen sulfide (H2S) and hydrogen cyanide (HCN) contained in the coke oven gas with sodium hydroxide, and leaving out the sodium hydrogen sulfide and sodium cyanide and discharging the rest of gases; second step of calculating a set value of proper sulfur content required for refining the cyanogen from the measured values using a control computer(70) after continuously measuring an amount of cyanogen (CN) absorbed from the absorption column; third step of discharging the sodium thiocyanate (NaSCN) after producing sodium hydroxide and sulfur and sodium thiocyanate (NaSCN) by transferring the sodium hydrogen sulfide and sodium cyanide remained in the absorption column to a regeneration column(20) and supplying compressed air, catalyst and Na2Sx+1 as much as an amount corresponding to the set value calculated in the control computer into the regeneration column; and fourth step of supplying the Na2Sx+1 into a sulfur balancing tank(60) and resupplying the supplied Na2Sx+1 as much as an amount corresponding to the set value calculated in the control computer into the regeneration column after transferring sulfur produced in the regeneration column into a buffer tank(30) and supplying sodium hydroxide and hydrogen sulfide into the buffer tank, thereby producing Na2Sx+1.
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机译:用途:一种优化反应的方法,其中通过预先计算除去焦炉煤气杂质氰所需要的硫含量并适当地保持湿法脱硫过程中的硫含量,将高毒性氰化钠通过硫转变为无害的硫氰酸钠提供。组成:湿法脱硫过程中炼焦炉气的方法包括第一步,将炼焦炉气和氢氧化钠(NaOH)供入吸收塔(10),通过反应生成硫化氢钠(NaHS)和氰化钠(NaCN)用氢氧化钠将焦炉煤气中所含的硫化氢(H 2 S)和氰化氢(HCN)除去,除去硫化氢钠和氰化钠,其余气体排出。第二步,是在连续测定从吸收塔吸收的氰(CN)的量后,用控制计算机(70)从测定值中求出精制氰所需要的适当硫含量的设定值。通过将残留在吸收塔中的硫化氢钠和氰化钠转移到再生塔(20)并供应压缩空气,催化剂和Na2Sx + 1等于再生计算机中控制计算机中计算出的设定值的数量;第四步是将Na 2 S x +1供应到硫平衡罐(60)中,然后将再生中产生的硫转移到再生塔中,再供应与控制计算机中计算出的设定值相对应的量的Na 2 S x +1。然后,将其通过柱子送入缓冲罐(30),并向缓冲罐中供给氢氧化钠和硫化氢,从而生成Na 2 S x +1。
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