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Fe2(SO4)3溶液吸收H2S废气工艺研究
引用本文:朱菊华,黄妍,童志权.Fe2(SO4)3溶液吸收H2S废气工艺研究[J].化工进展,2004,23(3):277-281.
作者姓名:朱菊华  黄妍  童志权
作者单位:湘潭大学环境工程系,湘潭,411105;湘潭大学环境工程系,湘潭,411105;湘潭大学环境工程系,湘潭,411105
基金项目:湖南省教委项目(01C581).
摘    要:报道了一种新型的硫化氢废气处理工艺,包括化学吸收和空气氧化两步。硫化氢被转化为单质硫。通过探讨废气流量、入口H2S浓度、吸收液初始Fe^3 ]、F3^2 ]、pH值、吸收液体积、温度等因素对脱硫率的影响,确定了硫酸铁体系适宜的反应条件。在实验室有限条件下脱硫率达92%以上。工业上进一步强化气液传质,脱硫率可望达98%以上。采用常压空气氧化法再生Fe^3 ,建立了“吸收-再生-吸收”循环体系。

关 键 词:硫酸铁  吸收  硫化氢  废气处理
文章编号:1000-6613(2004)03-0277-05
修稿时间:2003年10月21

Study on Abatement of H2S by Absorption in Ferric Solution
Zhu Juhua,Huang Yan,Tong Zhiquan.Study on Abatement of H2S by Absorption in Ferric Solution[J].Chemical Industry and Engineering Progress,2004,23(3):277-281.
Authors:Zhu Juhua  Huang Yan  Tong Zhiquan
Abstract:A novel process for abatement of hydrogen sulfide from gas streams is introduced, based on the combined action of a chemical absorption step and an oxidation step.In this process,H 2S is converted to sulfur. In order to determine the operating conditions of the system, effects of waste-gas flow, inlet H 2S concentration, concentration and volume of ferric solution, pH values, reacting temperature on desulfurization efficiency were investigated. The removal rate can reach 92 per cent under the laboratory condition, and can be further increased to more than 98 per cent in industry. Regenerating ferric ion by air oxidation under normal pressure, we established the recycle system of Absorption-Regeneration-Absorption.
Keywords:ferric sulfate  absorption  hydrogen sulfide  waste gas treatment  
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