Water-selective Membrane from Crosslinking of Poly(vinyl alcohol) with Tartaric Acid and Its Pervaporation Separation Characteristics for a Water/Acetic Acid Mixture
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Chaudhari, Shivshankar
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Kwon, YongSung
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Moon, MyngJun
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Pukyong Natl Univ, Dept Ind Chem, Busan 608739, South KoreaPukyong Natl Univ, Dept Ind Chem, Busan 608739, South Korea
Moon, MyngJun
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Shon, MinYoung
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Pukyong Natl Univ, Dept Ind Chem, Busan 608739, South KoreaPukyong Natl Univ, Dept Ind Chem, Busan 608739, South Korea
Shon, MinYoung
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Park, YouIn
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Korea Res Inst Chem Technol, Ctr Membranes, Taejon 305600, South KoreaPukyong Natl Univ, Dept Ind Chem, Busan 608739, South Korea
Park, YouIn
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Song, HyeRim
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Korea Res Inst Chem Technol, Ctr Membranes, Taejon 305600, South KoreaPukyong Natl Univ, Dept Ind Chem, Busan 608739, South Korea
Song, HyeRim
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Jang, BongJun
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Nam, SeungEun
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[1] Pukyong Natl Univ, Dept Ind Chem, Busan 608739, South Korea
[2] Korea Res Inst Chem Technol, Ctr Membranes, Taejon 305600, South Korea
The preparation of a water-selective membrane from the crosslinking of high molecular weight poly(vinyl alcohol) (PVA) with tartaric acid is reported. The resulting membrane was characterized by IR spectroscopy, swelling studies, differential scanning calorimetry, and contact angle testing, and was finally applied in the pervaporation. The performance of the membrane was evaluated in relation to the mixing ratio, changes in feed concentration, and changes in operating temperature. An optimum mixing ratio of 80:20 (wt %) of PVA to tartaric acid was determined, giving a flux range from 0.0072 to 0.095kg/m(2)h and a separation factor of 41.5-707.6 at 40-60 degrees C and 80-90wt % aqueous acetic acid feed solution. From an Arrhenius type of relationship, it was determined that flux varies exponentially with temperature. The activation energy was calculated for the permeation of each of component of the mixture, with a higher activation energy being observed for acetic acid than for water. From the separation index, it could be concluded that the membrane has good selectivity toward water and exhibits better performance at higher acetic acid concentrations.
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Nagoya Univ, Grad Sch Engn, Dept Chem Syst Engn, Chikusa Ku, Nagoya, Aichi 4648603, JapanNagoya Univ, Grad Sch Engn, Dept Chem Syst Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
Kunishi, Hiroto
Hagio, Takeshi
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Nagoya Univ, Grad Sch Engn, Dept Chem Syst Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
Nagoya Univ, Inst Mat Innovat, Inst Innovat Future Soc, Chikusa Ku, Nagoya, Aichi 4648601, JapanNagoya Univ, Grad Sch Engn, Dept Chem Syst Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
Hagio, Takeshi
Wada, Shintaro
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Nagoya Univ, Sch Engn, Dept Mat Sci & Engn, Chikusa Ku, Nagoya, Aichi 4648603, JapanNagoya Univ, Grad Sch Engn, Dept Chem Syst Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
Wada, Shintaro
Kamimoto, Yuki
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Nagoya Univ, Grad Sch Engn, Dept Chem Syst Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
Nagoya Univ, Inst Mat Innovat, Inst Innovat Future Soc, Chikusa Ku, Nagoya, Aichi 4648601, JapanNagoya Univ, Grad Sch Engn, Dept Chem Syst Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
Kamimoto, Yuki
Ichino, Ryoichi
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Nagoya Univ, Grad Sch Engn, Dept Chem Syst Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
Nagoya Univ, Inst Mat Innovat, Inst Innovat Future Soc, Chikusa Ku, Nagoya, Aichi 4648601, JapanNagoya Univ, Grad Sch Engn, Dept Chem Syst Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan