中空纤维膜溶剂吸收烟气脱硫研究
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摘要
采用自制的微孔聚丙烯中空纤维膜组件为膜吸收反应器,以Na_2SO_3溶液为吸收液,对中空纤维膜溶剂吸收烟气脱硫进行了实验研究。考察了吸收液性质、进气气速和膜组件结构参数等对分离过程和效率的影响,在理论和实验的基础上,研究了孔径、膜传质系数和脱硫效率之间的关系。实验结果表明,当吸收液pH值>7时脱硫率最大,且保持稳定;吸收液浓度≥5%时,吸收液的液相阻力可以忽略;膜组件脱硫率随气速的增大而减小,而随膜组件有效长度、膜传质系数的增大而增大;膜孔径大易产生润湿现象。分别利用传质经验式和传质微分方程推导建立了非润湿性中空纤维膜组件脱硫效率传质模型,模拟结果与实验数据吻合较好。
An experimental research of FGD by hollow-fiber membrane-based absorption system was carried out, the hollow-fiber microporous membrane modules were used as membrane contactors and the aqueous solution of sodium sulfite was chosen as the absorbent. The effect of characteristics on desulfurization efficiency have been widely investigated, the relation of pore size, the membrane's coefficient and the desulfurization efficiency have been also examined both theoretically and experimentally. The results show that, when pH of absorbent is more than 7, the desulfurization efficiency is best and constant, concentration of absorbent is more than 5%, the mass-transfer resistance of the liquid is negligible, Increasing the effective length of module and the membrane's coefficient will help to increase the desulfurization efficiency of module but velocity of feed gas, and the larger pore size makes membrane leak easily. The mathematical model of desulfurization efficiency in hydrophobic hollow-fiber membrane was set up
    respectively by using of the mass transfer empirical correlation and differential equation. The results from the model are in good agreement with the experimental data.
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