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作 者:李睿[1] 徐军[1] 许志良[1] 王连军[1] 李健生[1] 孙秀云[1]
出 处:《环境工程学报》2008年第9期1194-1198,共5页Chinese Journal of Environmental Engineering
基 金:江苏省省级环保科技项目(2005005)
摘 要:以C6H6/N2混合气为代表,疏水性聚丙烯中空纤维膜为气液接触膜,n-甲酰吗啉(NFM,n-formylmorpholine)水溶液为吸收剂,研究了膜气体吸收法分离VOCs/N2混合气性能。考察了吸收剂流量、吸收剂体积分数、进口气流量、进口气浓度和膜组件结构等诸因素对分离性能的影响。结果表明,在吸收剂流量为20~100mL/min,进口气流量为40~300mL/min,进口气浓度为10.2mg/L的条件下,苯的去除率为65.0%~99.6%,总体积传质系数为0.0157~0.08412s-1。实验证明,采用疏水性多孔膜气体吸收法,NFM水溶液吸收分离VOCs/N2混合气具有较高的分离效率和较快的传质速率。The work focuses on a membrane based gas absorption process for the separation VOCs from N2- Benzene was chosen as the target VOCs and the aqueous solution of n-formyl morpholine (NFM) was used as ab- sorbent. Mass-transfer performance of separation benzene was studied in the hollow fiber polypropylene membrane (HFPPM). Effect of various factors, including flowrate of absorbent and feeding gas, concentration of ab- sorbent and feeding gas, differences of membranes modules on the efficiency of benzene absorption were investi- gated. The results show that the removal efficiency achieves 65.0 % - 99.6 % and the overall volume transfer coefficient achieves 0. 0157 - 0. 08412 s-1, when following conditions were used: concentration of feed gas, 10.2 mg/L; flowrate of absorbent, 20- 100 mL/min; flowrate of feed gas, 40 -300 mL/min. The characteristics of separation of VOCs/N2 by membrane contactor are of quicker mass transfer velocity and higher efficiency of separation.
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