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    阮雪华

    • 教授     博士生导师   硕士生导师
    • 任职 : 辽宁省工业VOCs综合治理及利用专业技术创新中心副主任
    • 性别:男
    • 毕业院校:大连理工大学
    • 学位:博士
    • 所在单位:化工海洋与生命学院
    • 学科:化学工程. 膜科学与技术. 水科学与技术
    • 办公地点:盘锦校区D01-316A
    • 电子邮箱:xuehuaruan@dlut.edu.cn

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    Further separation of HFC-23 and HCFC-22 by coupling multi-stage PDMS membrane unit to cryogenic distillation

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    论文类型:期刊论文

    发表时间:2015-12-17

    发表刊物:SEPARATION AND PURIFICATION TECHNOLOGY

    收录刊物:SCIE、EI、Scopus

    卷号:156

    页面范围:673-682

    ISSN号:1383-5866

    关键字:Fluoroform; Membrane; Gas separation; Global warming; Optimization

    摘要:Fluoroform (HFC-23), the unavoidable byproduct of chlorodifluoromethane (lCFC-22) synthesis, is one of the most potent greenhouse gases. The general approach to incinerate the vent gas, though avoids the adverse environmental impacts, is a waste of HFC-23, which is valuable as refrigerant and plasma etchant. In this work, membrane process was coupled with distillation to separate high purity HFC-23 from the vent gas economically. Theoretical analysis and experimental tests were conducted to find the applicable membrane materials. The results indicated that the rubbery PDMS, with higher selectivity and gas permeation coefficients, was superior to the glassy PI for HFC-23 separation. PDMS thin-film composite membranes were prepared and characterized. In the actual permeation tests with industrial vent gas at 30 degrees C and 0.55 MPa, the as-prepared PDMS composite membranes behaved with selectivity alpha(F22/F23) = 3.2 and permeation rate J(F22) = 661 GPU, respectively. Afterwards, the cascaded membrane systems with different stage number were studied by process simulation and their economic feasibility was analyzed. Briefly according to the economic data, the 4-stage cascade structure is the optimal configuration to couple with distillation unit. For a 50 kt/a synthesis plant, the 4-stage process can efficiently refine HFC-23 to a purity as high as 99.5 mol%, with a specific cost of 70 USD t(-1) and an extra gross profit of 3.8 x 10(6) USD a(-1). However, taking the process complexity into account, the 3-stage cascaded process, although exhibited slightly lower economic performance, is more suitable in industry. Overall, our studies have revealed that coupling PDMS membrane unit with distillation is a feasible and promising technique to separate high purity HFC-23 efficiently and economically in the HCFC-22 synthesis industries. (C) 2015 Elsevier B.V. All rights reserved.