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Pervaporation separation of water–acetic acid mixtures through poly(vinyl alcohol)-silicone based hybrid membranes
Institution:1. Chemical Process Engineering, University of Oulu, P.O. Box 4300, FI-90014 University of Oulu, Finland;2. College of Life Sciences, Hebei Agricultural University, Baoding 071001, Hebei, China;3. School of Forest Sciences, University of Eastern Finland, P.O. Box 111, FI-80101 Joensuu, Finland;1. Division of Physical Science, Materials Science Program, Faculty of Science, Prince of Songkla University, 90112, Thailand;2. Division of Physical Science, Physics Program, Faculty of Science, Prince of Songkla University, 90112, Thailand;3. Cernter of Excellent in Membrane Science and Technology (CoE-MST), Prince of Songkla University, 90112, Thailand;1. Department of Chemical and Biological Engineering, Zhejiang University, Hangzhou 310027, PR China;2. MOE Engineering Research Center of Membrane and Water Treatment Technology, Zhejiang University, Hangzhou 310027, PR China;3. Department of Chemical and Biomolecular Engineering, University of Delaware, Newark, DE 19716, USA;1. Department of Ocean, Zhejiang University of Technology, Hangzhou, 310014, China;2. College of Chemical Engineering, Zhejiang University of Technology, Hangzhou, 310014, China;3. Department of Chemistry, Zhejiang University, Hangzhou, 310012, China;4. Huzhou Institute of Collaborative Innovation Center for Membrane Separation and Water Treatment, 1366 Hong Feng Road, Huzhou, 313000, China
Abstract:Hybrid membranes were prepared using poly(vinyl alcohol) (PVA) and tetraethylorthosilicate (TEOS) via hydrolysis followed by condensation. The obtained membranes were characterized by Fourier transform infrared spectroscopy, wide-angle X-ray diffraction and differential scanning calorimetry. The remarkable decrease in degree of swelling was observed with increasing TEOS content in membranes and is attributed to the formation of hydrogen and covalent bonds in the membrane matrix. The pervaporation performance of these membranes for the separation of water–acetic acid mixtures was investigated in terms of feed concentration and the content of TEOS used as crosslinking agent. The membrane containing 1:2 mass ratio of PVA and TEOS gave the highest separation selectivity of 1116 with a flux of 3.33 × 10−2 kg/m2 h at 30 °C for 10 mass% of water in the feed. Except for membrane M-1, the observed values of water flux are close to the values of total flux in the investigated composition range, signifying that the developed membranes are highly water selective. From the temperature dependence of diffusion and permeation values, the Arrhenius apparent activation parameters have been estimated. The resulting activation energy values, obtained for water permeation being lower than those of acetic acid permeation values, suggest that the membranes have higher separation efficiency. The activation energy values calculated for total permeation and water permeation are close to each other for all the membranes except membrane M-1, signifying that coupled-transport is minimal as due to higher selective nature of membranes. Further, the activation energy values for permeation of water and diffusion of water are almost equivalent, suggesting that both diffusion and permeation contribute almost equally to the pervaporation process. The negative heat of sorption values (ΔHs) for water in all the membranes suggests the Langmuir's mode of sorption.
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