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

机译:多相反应器中工业生产硫酸钠(NaHS 43%)水溶液

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Background: 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%. Methods: 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%. Results: 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. Conclusion: 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.
机译:背景:这项研究涉及在等温多相化学反应器中生产硫化钠和亚硫酸钠,以通过硫化氢和钠的氢氧化物在50℃下的气液固反应生产浓水合硫酸钠水溶液(大于43%)。 %。方法:提出了一种方法,该方法整合了从工业化学过程中回收硫化氢的过程,在该过程中,产生的H2S气体是副产品,将开发过程的策略整合到二硫代磷酸(ADTF)的生产工厂中。可以回收浓度高于43%的NaHS水溶液形式的硫化氢。结果:实验测试表明,由Na2S,NaHS和H2O形成的两相反应混合物的整体组成为13.3%。在搅拌釜式反应器中,分别得到26.9%和59.7%的水合硫酸钠是合适的,反应器在50°C至55°C的温度范围内操作,其中不断鼓入气态硫化氢。结论:两相混合物的硫化钠(特别是Na2S.5H2O晶体)是由水合硫酸钠(43%NaHS)和氢氧化钠水溶液(50%NaOH)制成的。 H2S产生的环境问题得到了解决,多相反应器的回收率为90%,安全吸收器的回收率为5%。

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