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Removal of thiophenes from n-octane/thiophene mixtures by pervaporation

机译:通过全蒸发从正辛烷/噻吩混合物中除去噻吩

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PDMS/PAN composite membrane was prepared and employed in pervaporation separation of n-octane/thiophene mixtures at laboratory scale. At different initial thiophenes (thiophene and 2-methyl-thiophene) concentrations (corresponding sulfur contents about 500-2500 mu g/g) and feed temperatures (30-70 degrees C), experimental results were carried out and average flux, selectivity and activation energy of permeation were calculated. It was found that increasing in temperature yields higher total fluxes and lower selectivity to thiophenes, while changing concentration of thiophens in the range concerned produces insignificant effect on total flux and selectivity. Experiments also showed that PDMS membrane is more selective to thiophene than to 2-methyl-thiophene and it may be mainly because of the difference in molecular size and structure. Total fluxes for thiophene-octane mixture and 2-methyl-thiophene-octane mixture were measured to be 1.5 and 1.4 kg/m(2) h at 30 degrees C, with the corresponding selectivity to thiophenes 4.9 and 2.5, respectively. Based on simplified solution-diffusion model, the permeation fluxes of individual components in pervaporation of thiophene/2-methyl-thiophene-octane ternary mixture had been predicted and showed to be in good agreement with experimental values. (c) 2005 Elsevier B.V. All rights reserved.
机译:制备PDMS / PAN复合膜,并用于实验室规模的正辛烷/噻吩混合物的全蒸发分离。在不同的初始噻吩(噻吩和2-甲基噻吩)浓度(相应的硫含量约500-2500μg / g)和进料温度(30-70摄氏度)下,进行了实验结果,并得出了平均通量,选择性和活化度计算渗透能。已经发现,温度升高产生较高的总通量和较低的噻吩选择性,而在相关范围内改变噻吩的浓度对总通量和选择性影响不大。实验还表明,PDMS膜对噻吩的选择性比对2-甲基噻吩的选择性大,这可能主要是由于分子大小和结构的差异。在30摄氏度下,噻吩/正辛烷混合物和2-甲基噻吩/正辛烷混合物的总通量分别为1.5和1.4 kg / m(2)h,分别对噻吩的选择性为4.9和2.5。 。基于简化的溶液扩散模型,预测了噻吩/ 2-甲基噻吩/正辛烷三元混合物全蒸发中各组分的渗透通量,与实验值吻合良好。 (c)2005 Elsevier B.V.保留所有权利。

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