CIESC Journal ›› 2005, Vol. 56 ›› Issue (11): 2059-2064.

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Mass transfer and kinetics of sulfite forced oxidation reaction

ZHAO Bo;LI Yan;TONG Huiling;ZHANG Xiaowen;ZHUO Yuqun;JIN Gangshan;CHEN Changhe   

  • Online:2005-11-25 Published:2005-11-25

亚硫酸盐强制氧化传递与化学反应动力学

赵博;李彦;佟会玲;张晓闻;禚玉群;金刚善;陈昌和   

  1. 清华大学热科学与动力工程教育部重点实验室,北京 100084

Abstract: Wet limestone scrubbing is the most common flue gas desulfurization process for control of sulfur dioxide emissions from the combustion of fossil fuels, and forced oxidation which belongs to gas-liquid transfer process is a key path of the reaction.In the present work,the two-film theory was used to analyze the sulfite forced oxidation reaction with an image boundary recognition technique and the oxidation rate was experimentally studied by contacting pure oxygen with a sodium sulfite solution.There was a critical sulfite concentration 0.328 mol•L-1 without catalyst or at a steady catalyst concentration.When the Co2+ catalyst concentration was kept unchanged, the sulfite oxidation reaction rate was controlled by dual film and the reaction kinetics was first order with respect to sulfite while SO2-3 concentration was below 0.328 mol•L-1.The sulfite oxidation reaction rate was controlled by gas film only and the reaction was zeroth order with respect to sulfite while the SO2-3 concentration was over 0.328 mol•L-1.When SO2-3 concentration was kept unchanged, the sulfite oxidation reaction rate depended on gas-liquid mass transfer and the reaction kinetics was different in various stages with respect to Co2+ concentrations.

Key words: 传质, 动力学, 氧化速率, 临界浓度

摘要: 在湿法烟气脱硫的过程中,吸收塔底部发生的反应主要是亚硫酸钙和空气或氧气之间的气液传递与化学反应过程,根据双膜理论模型,分析了该反应的吸收机理,用一种图像边界识别的方法分析亚硫酸盐强制氧化气液反应.在没有催化剂或固定钴离子催化剂浓度时,SO2-3存在临界浓度0.328 mol•L-1.当SO2-3的浓度低于0.328 mol•L-1时,过程为双膜控制,SO2-3的反应级数为1;当SO2-3的浓度大于0.328 mol•L-1时,过程逐渐变为气膜控制,SO2-3反应级数为0.当固定SO2-3浓度时,催化剂钴离子的反应级数则受到气液传质的影响,分为几个阶段,且反应级数不同.

关键词: 传质, 动力学, 氧化速率, 临界浓度