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Crosslinked Nanocomposite Sodium Alginate-Based Membranes with Titanium Dioxide for the Dehydration of Isopropanol by Pervaporation

机译:TiO2交联的纳米复合藻酸钠基膜与异丙醇的全蒸发脱水

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摘要

Sodium alginate (NaAlg) based membranes were prepared using a solution technique, crosslinked with poly(styrene sulfonic acid-co-maleic acid) (PSSA-co-MA). Subsequently, the membranes were modified by the incorporation of 0, 10, 20, 30 and 40% / of titanium dioxide with respect to sodium alginate. The membranes thus obtained were designated as M, M-1, M-2, M-3 and M-4, respectively. An equilibrium swelling experiment was performed using different compositions of the water and isopropanol mixtures. Subsequently, we used a pervaporation cell fitted with each membrane in order to evaluate the extent of the pervaporation dehydration of isopropanol. Among the membranes studied, the membranes containing 40 mass% of titanium dioxide exhibited the highest separation factor(α) of 24,092, with a flux(J) of 18.61 × 10 kg/m ∙h at 30 °C for 10 mass% / of water in the feed. The total flux and the flux of water were found to overlap with each other, indicating that these membranes can be effectively used to break the azeotropic point of water–isopropanol mixtures. The results clearly indicate that these nanocomposite membranes exhibit an excellent performance in the dehydration of isopropanol. The activation energy values obtained for the water permeation were significantly lower than those of the isopropanol permeation, underlining that these membranes have a high separation ability for the water–isopropanol system. The estimated activation energies for total permeation (E ) and total diffusion (E ) values ranged between 10.60 kJ∙mol and 3.96 kJ∙mol , and 10.76 kJ∙mol and 4.29 kJ∙mol , respectively. The negative change in the enthalpy values for all the membranes indicates that sorption was mainly dominated by Langmuir’s mode of sorption.
机译:使用溶液技术制备海藻酸钠(NaAlg)基膜,并与聚(苯乙烯磺酸-顺丁烯二酸)(PSSA-co-MA)交联。随后,通过掺入相对于藻酸钠为0、10、20、30和40%的二氧化钛来修饰膜。这样获得的膜分别命名为M,M-1,M-2,M-3和M-4。使用不同组成的水和异丙醇混合物进行了平衡溶胀实验。随后,我们使用装有各膜的全蒸发池,以评估异丙醇的全蒸发脱水程度。在所研究的膜中,含有40质量%的二氧化钛的膜表现出最高的分离因子(α)为24,092,在30°C时10(质量)%的通量(J)为18.61×10 kg / m∙h。饲料中加水。发现总通量和水通量彼此重叠,表明这些膜可有效地用于打破水-异丙醇混合物的共沸点。结果清楚地表明,这些纳米复合膜在异丙醇的脱水中表现出优异的性能。水渗透获得的活化能值明显低于异丙醇渗透的活化能值,这说明这些膜对水-异丙醇系统具有很高的分离能力。总渗透率(E)和总扩散率(E)的估计活化能分别在10.60 kJ∙mol和3.76 kJ∙mol之间以及10.76 kJ∙mol和4.29 kJ∙mol之间。所有膜的焓值均呈负变化,表明吸附主要由Langmuir的吸附方式决定。

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