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纯溶剂在线性低密度聚乙烯膜中扩散的计算

Calculation of diffusion behavior of pure solvents through linear low-density polyethylene(LLDPE) membrane
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摘要 为了评价和预测密封材料线性低密度聚乙烯(LLDPE)的防渗透性能,结合实验和数学模型2种手段,研究5种化工溶剂在LLDPE薄膜中的扩散性能.采用稳态渗透汽化实验和吸附溶胀实验分别获得各组分的渗透通量数据和平衡吸附量.引入Fujita自由体积模型阐述扩散系数,根据渗透通量实验数据拟合得到各组分的自由体积参数.结果表明,渗透通量的计算值与实验值基本一致.根据模型计算得到5种溶剂的扩散系数随温度变化的曲线.通过求解Fick第二定律的偏微分方程数值解,得到不同时刻5种溶剂在平板膜内部的质量浓度分布曲线.结果表明,LLDPE对5种溶剂的防渗透性能良好. The diffusion behaviors of five kinds of pure solvents through LLDPE membrane were investigated by experimental and numerical methods in order to evaluate and predeterminate the anti-infiltration performances of linear low-density polyethylene(LLDPE) sealing material.The permeation flux and equilibrium absorption capacity in the LLDPE membrane were obtained from steady pervaporation experiments and swelling experiments respectively.The diffusion coefficient was described by Fujita free volume theory and the parameters in the model were obtained by fitting a numerical solution of the flux equation to experimental data.The calculated fluxes using the free volume model accorded well with experimental results.The calculated diffusion coefficients for five kinds of solvents in LLDPE at different temperatures were drawn based on the mathematical model.Mass concentration distribution curves for five kinds of solvents in the plate membrane were calculated by numerically solving the partial different equation of Fick's second law.Results showed that LLDPE material had excellent anti-infiltration performances for five solvents.
出处 《浙江大学学报(工学版)》 EI CAS CSCD 北大核心 2012年第4期744-748,776,共6页 Journal of Zhejiang University:Engineering Science
基金 国家"十一五"科技支撑资助项目(2007BAD75B05) 广西大学博士启动基金资助项目(XBZ110452) 广西石化资源加工及过程强化技术重点实验室开放基金资助项目(K012)
关键词 渗透汽化 线性低密度聚乙烯(LLDPE) 自由体积模型 溶解扩散模型 FICK第二定律 pervaporation linear low-density polyethylene(LLDPE) free volume model solution-diffusion model Fick's second law
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参考文献15

  • 1JANSSON S E A, GALLET G, HEFTI T, et al. Packaging materials for fermented milk, Part 2: soluteinduced changes and effects of material polarity and thickness on food quality [J]. Packaging Technology and Science, 2002, 15(6): 287-300.
  • 2LUTZOW N, TIHMINLIOGLU A, DANNER R P, et al. Diffusion of toluene and nheptane in polyethylenes of different crystallinity [J]. Polymer, 1999, 40(10): 2797-2803.
  • 3蒋文华,韩世钧.3种芳香烃在聚乙烯膜中的无限稀释扩散系数[J].化工学报,2002,53(3):285-289. 被引量:1
  • 4朱丽芳,蔡邦肖,高从堦,王邵雷.渗透汽化膜分离MeOH/MTBE混合物的传质分析——单组分在膜中的扩散[J].化工学报,2003,54(2):164-169. 被引量:5
  • 5FUJITA H. Diffusion in polymerdiluent systems [J]. Fortschr Hochpolym Forsch, 1961, 3(1): 1-47.
  • 6HONG S. Prediction of polymer/solvent diffusionbehavior using freevolume theory [J]. Industrial and Engineering Chemistry Research, 1995, 34(7): 2536-2544.
  • 7赵欣,李继定,陈剑,陈翠仙.改进的Vrentas-Duda扩散模型及其应用 (Ⅰ)预测弱极性分子在聚合物膜中的扩散系数[J].膜科学与技术,2003,23(6):8-13. 被引量:5
  • 8LIU K, TONG Z, LIU L, et al. Separation of organic compounds from water by pervaporation in the production of nbutyl acetate via esterification by reactive distillation [J]. Journal of Membrane Science, 2005, 256(1): 193–201.
  • 9SHAO P, HUANG R Y M. Review polymeric membrane pervaporation [J]. Journal of Membrane Science, 2007, 287(2): 162-179.
  • 10WIJMANS J G, BAKER R W. The solutiondiffusion model: a review [J]. Journal of Membrane Science, 1995, 107(1): 1-21.

二级参考文献73

  • 1马沛生,赵兴民,李平,郭洁.基团法估算溶度参数[J].石油化工,1994,23(9):593-597. 被引量:7
  • 2陈翠仙 李继定.渗透汽化膜传递理论研究的进展[A].清华大学化工系编.第三届全国膜和膜过程学术报告会论文集[C].北京,1999.2~6.
  • 3Wijmans J G, Baker R W. The solution-diffusion model: a review [J]. Journal of Membrane Science, 1995, 107(1): 11-21.
  • 4Liu K, Tong Z, Li Let al. Separation of organic compounds from water by pervaporation in the production of n-butyl acetate via esterification by reactive distillation [J]. Journal of Membrane Science, 2005, 256(1 ): 193-201.
  • 5Liu L, Chakma A, Feng X. A novel method of preparing ultrathin poly(ether block amide) membranes [J]. Journal of Membrane Science, 2004, 235(1): 43-52.
  • 6Mulder M H Y, Smolders C A. On the mechanism of separation of ethanol/water mixtures by pervaporation: Calculation of concentration profiles [J]. Journal of Membrane Science, 1984, 17(3): 289-307.
  • 7Enneking L, Heintz A, Lichtenthaler R N. Sorption equilibria of the ternary mixture benzene/ cyclohexen/ cyclohexane in polyurethane and PEBA membrane polymer [J]. Journal of Membrane Science, 1996, 115(2): 161-170.
  • 8Lindvig T, Michelsen M L, Kontogeorgis G M. A Flory-Huggins model based on the Hansen solubility parameters [J]. Fluid Phase Equilibria, 2002, 203(1-2): 247-260.
  • 9Hong S U. Prediction of polymer/solvent diffusion behavior using flee-volume theory [J]. Ind Eng Chem Res, 1995, 34(7): 2536-2544.
  • 10Heintz A, Stephan W A generalized solution-diffusion model of the pervaporation process through composite membranes. Part l. Prediction of mixture solubilities in the dense active layer using the UNIQUAC model [J]. Journal of Membrane Science, 1994, 89(1-2): 143-151.

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