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响应面优化法在PDMS/PVDF膜制膜条件优化中的应用

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    2024-6-10 16:33
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    发表于 2012-10-13 14:50:58 | 显示全部楼层 |阅读模式
    响应面优化法在PDMS/PVDF膜制膜条件优化中的应用
    Application of Response Surface Methodology(RSM) to Optimize the Preparation  Conditions of PDMS/PVDF Composite Membranes

    作  者:樊铖 展侠 陈剑 潘福生 秦琳 王涛 李继定

    FAN Cheng, ZHAN Xia, CHEN Jian, PAN Fu-sheng, QIN Lin, WANG Tao, LI Ji-ding  (The State Key Laboratory of Chemical Engineering, Department of Chemical Engineering,  Tsinghua University, Beijing 100084, China)

    机构地区:清华大学化学工程国家重点联合实验室,北京100084

    出  处:《高校化学工程学报》 EI CAS CSCD 2012年第26卷第3期 374-381页,共8页

    Journal of Chemical Engineering of Chinese Universities

    基  金:国家973项目(2009CB623404); 国家自然科学基金项目(20736003)

    摘  要:用响应面优化法优化了乙烯基封端PDMS/PVDF渗透汽化透醇膜的制膜条件,研究了硅橡胶浓度、B/A质量比、交联温度和交联时间对膜性能的影响,拟合了分离因子、渗透通量与四因素之间的回归方程,并用方差分析法考察了四因素的主效应、二次效应以及相互作用效应对复合膜的分离因子与渗透通量的影响。研究发现,硅橡胶浓度对膜的分离因子与渗透通量的影响最为显著,交联时间对分离因子几乎没有影响。通过对回归方程的优化分析得知,在料液乙醇浓度为10%(wt),操作温度40℃条件下,当硅橡胶浓度为93%(wt),B/A质量比为0.08,交联温度为100℃,交联时间为13.83 h时,膜的综合分离性能达到最佳,此时分离因子与渗透通量预测值分别为9.47、77.57 g(m2 h)1,渗透侧乙醇浓度达到51.3%(wt)。回归方程的验证实验结果表明,回归方程的估计值与实验值较为吻合,可用于乙烯基封端的PDMS/PVDF复合膜的渗透汽化性能的预测与优化。

    The response surface methodology (RSM) was used to optimize the preparation conditions of PDMS/PVDF composite membranes for pervaporation. The effects of four variables including silicone rubber concentration, mass ratio of RTV B to RTV A, cross-linking temperature and time on the membrane performances were investigated. The regression equations between the preparation variables and the performances of the composite membranes were established, and the main effects, quadratic effects and the effects of interactions of the four variables on the separation factor and permeation flux of the composite membranes were studied. It was found that the silicone rubber concentration affects the selectivity and permeation flux of the composite membranes prepared most significantly, while the cross-linking time has almost no effect on the selectivity. According to the optimization analysis of the proposed regressing equation, it was found that, at 40℃ and ethanol concentration of 10%(wt) and when the silicone concentration is 93%(wt), the mass ratio ofRTV B to RTV A is 0.08, cross-linking temperature is 100℃ and cross-linking time is 13.83 h, the prepared PDMS/PVDF composite membrane will have the optimum performances of selectivity of 9.47, total flux of 77.57 g·(m2·h)-1 and the ethanol concentration of the permeate side is 51.3%. The experimental results are in good agreement with those predicated by the proposed regression equation, which indicates that the proposed regression equation could be used to forecast and optimize the pervaporation performance of the PDMS/PVDF composite membrane to be prepared.

    关 键 词:PDMS 星点设计 响应面优化法 渗透汽化 透醇膜
    PDMS central composite design response surface methodology pervaporation ethanol-selective membrane
    分 类 号:TQ028.8 [工业技术 > 化学工业 > 一般性问题 > 化工过程(物理过程及物理化学过程) > 分离过程] TQ021.8 [工业技术 > 化学工业 > 一般性问题 > 化工过程(物理过程及物理化学过程) > 基础理论]

    参考文献作者在撰写文献时引用的其他文献,反映本文的背景或依据。 (24篇)[1]徐玲芳 相里粉娟 陈祎玮 等.渗透汽化在生物燃料乙醇制备中的研究进展[J].化工进展,2007,26(6):788-796.
    [2]Brien D J,Roth L H,McAloon A J.Ethanol production by continuous fermentation–pervaporation:a preliminary economic analysis[J].J Membr Sci,2000,166(1):105-111.
    [3]Yi S L,Su Y,Qi B K,et al.Application of response surface methodology and central composite rotatable design in optimizing thepreparation conditions of vinyl-triethoxysilane modified silicalite/polydimethylsiloxane hybrid pervaporation membranes[J].SepPurif Technol,2010,71(2):252-262.
    [4]TANGXiao-yu(汤晓玉) ZHOUYi-hui(周一慧) YUANLin(原林) etal.Membrane Separation Performance for Apple JuiceFermentation in a Silicone Rubber Membrane Bioreactor(硅橡胶膜生物反应器在苹果原汁发酵过程中的膜分离性能)[J].高校化学工程学报,2010,24(1):76-81.
    [5]伍勇 肖泽仪 黄卫星 钟月华.乙醇发酵与渗透汽化在硅橡胶膜生物反应器中的耦合强化[J].高校化学工程学报,2004,18(2):241-245.
    [6]Mohammadi T,Aroujalian A,Bakhshi A.Pervaporation of dilute alcoholic mixtures using PDMS membrane[J].Chem Eng Sci,2005,60(7):1875-1880.
    [7]Li L,Xiao Z,Tan S,et al.Composite PDMS membrane with high flux for the separation of organics from water by pervaporation[J].J Membr Sci,2004,243(1-2):177-187.
    [8]Fadeev A G,Kelley S S,McMillan J D,et al.Effect of yeast fermentation by-products on poly[1-(trimethylsilyl)-1-propyne]pervaporative performance[J].J Membr Sci,2003,214(2):229-238.
    [9]Bowen T C,Meier R G,Vane L M.Stability of MFI zeolite-filled PDMS membranes during pervaporative ethanol recovery fromaqueous mixtures containing acetic acid[J].J Membr Sci,2007,298(1-2):117-125.
    [10]Ulutan S,Nakagawa T.Separability of ethanol and water mixtures through PTMSP–silica membranes in pervaporation[J].J MembrSci,1998,143(1-2):275-284.
    [11]Ikegami T,Kitamoto D,Negishi H,et al.Drastic improvement of bioethanol recovery using a pervaporation separation techniqueemploying a silicone rubber-coated silicalite membrane[J].J Chem Technol Biotechnol,2003,78(9):1006-1010.
    [12]Vane L M.A review of pervaporation for product recovery from biomass fermentation processes[J].J Chem Technol Biotechnol,2005,80(6):603-629.
    [13]Zhan X,Li J D,Huang J Q,et al.Pervaporation properties of PDMS membranes cured with different cross-linking reagents forethanol concentration from aqueous solutions[J].Chin J Polym Sci,2009,27(4):533-542.
    [14]Vane L M,Namboodiri V V,Bowen T C.Hydrophobic zeolite–silicone rubber mixed matrix membranes or ethanol/water separation:Effect of zeolite and silicone component selection on pervaporation performance[J].J Membr Sci,2008,308(1-2):230-241.
    [15]Xiangli F J,Wang W,Chen Y W,et al.Optimization of preparation conditions for polydimethylsiloxane(PDMS)/ceramic compositepervaporation membranes using response surface methodology[J].J Membr Sci,2008,311(1-2):23-33.
    [16]Garcia V,Landaburu-Aguirre J,Pongracz E,et al.Dehydration of water/dichloromethane/n-butanol mixtures by pervaporationptimisation and modelling by response surface methodology[J].J Membr Sci,2009,338(1-2):111-118.
    [17]Box G E P,Wilson K B.On the experimental attainment of optimal conditions[J].J Roy Stat Soc B,1951,13(1):1-45.
    [18]MABao-sheng(马宝胜).[D].Beijing(北京):Beijing University of Technology(北京工业大学),2007.
    [19]Idris A,Kormin F,Noordin M Y.Application of response surface methodology in describing the performance of thin film compositemembrane[J].Sep Purif Technol,2006,49(3):271-280.
    [20]Montgomery D C.Design and Analysis of Experiments[M].6th ed,New York,USA:John Wiley&Sons,2006.
    [21]Zhan X,Li J D,Chen J,et al.Pervaporation of ethanol/water mixtures with high flux by zeolite-filled PDMS/PVDF compositemembranes[J].Chin J Polym Sci,2009,27(6):771-780.
    [22]Chen C X,Han B B,Li J D,et al.A new model on the diffusion of small molecule penetrants in dense polymer membranes[J].JMembr Sci,2001,187(1-2):109-118.
    [23]Esteves A C C,Brokken-Zijp J,Laven J,et al.Influence of cross-linker concentration on the cross-linking of PDMS and the networkstructures formed[J].Polym,2009,50(16):3955-3966.
    [24]Liang L,Dickson J M,Zhu Z,et al.Removal of 1,2-dichloroethane from aqueous solutions with novel composite polydimethylsiloxanepervaporation membranes[J].J Appl Polym Sci,2005,98(4):1477-1491.

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    响应面优化法在PDMS/PVDF膜制膜条件优化中的应用

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