Industrial Manufacturing of Aqueous Solutions of Sodium Sulfhydrate (NaHS 43%) in a Multi-Phase Reactor

Warren Réategui-Romero, Fredy Castillejo-Melgarejo, María E. King-Santos
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引用次数: 3

Abstract

This research deals with the manufacture of sodium sulphides and sodium sulfhydrate in an isothermal multiphase chemical reactor to produce concentrated aqueous solutions of sodium sulfhydrate (greater than 43%) through Gas-Liquid-Solid reactions from hydrogen sulfide and hydroxide of sodium at 50%. A method is proposed that integrates the recovery of hydrogen sulfide from an industrial chemical process where the H2S gas is generated as a sub product, the strategy of the developed process was integrated into a manufacturing plant of dithiophosphoric acids (ADTF) where it was possible to recover the hydrogen sulfide in the form of an aqueous solution of NaHS with a concentration higher than 43%. The experimental tests showed that the biphasic reaction mixture formed by Na2S, NaHS and H2O with global compositions of 13.3%; 26.9% and 59.7% respectively, is appropriate to obtain 43% sodium sulfhydrate in a stirred tank reactor, operated at temperatures ranging from 50°C to 55°C, where gaseous hydrogen sulfide is continually bubbled. Sodium sulfide (specifically Na2S.5H2O crystals) of the biphasic mixture is produced from a solution of sodium sulfhydrate (43% NaHS) and aqueous sodium hydroxide (50% NaOH). The environmental problem generated by the H2S was solved with a 90% recovery in the multiphase reactor and 5% in the safety absorber.
多相反应器中水合硫酸钠(NaHS 43%)水溶液的工业生产
本研究是在等温多相化学反应器中,以硫化氢和50%的氢氧化钠为原料,通过气-液-固反应制备硫化钠和水合硫酸钠的浓缩水溶液(大于43%)。提出了一种从工业化学过程中回收硫化氢的方法,其中H2S气体作为子产物产生,并将该开发过程的策略集成到二硫代磷酸(ADTF)制造工厂中,在该工厂中可以回收浓度高于43%的NaHS水溶液形式的硫化氢。实验结果表明:Na2S、NaHS和H2O形成的双相反应混合物,总成分为13.3%;在50℃~ 55℃的搅拌釜反应器中,气态硫化氢连续起泡,得到43%的硫化钠是合适的。硫化钠(特别是Na2S)。两相混合物中的5H2O晶体)是由水合硫酸钠(43% NaHS)和氢氧化钠水溶液(50% NaOH)的溶液产生的。H2S在多相反应器中回收率为90%,在安全吸收器中回收率为5%,解决了H2S产生的环境问题。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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