Polymer(Korea), Vol.16, No.1, 85-93, January, 1992
아크릴산-아크릴로니트릴 공중합체막을 이용한 물-초산 혼합물의 투과증발분리
Prevaporation Separation of Water-Acetic Acid Mixture Through Poly(acrylic acid-co-acrylonitrile) Membrane
초록
친수성 작용기를 가진 고분자막으로 투과증발분리법을 사용하여 물/아세트산 혼합물의 분리를 시행하였다. 고분자막은 poly(acrylic acid-co-acrylonitrile)[Poly(AA-co-AN)]로 부터 제조하였다. 일반적으로, 카르복시기와 같은 친수성 작용기들은 물/유기물 혼합물의 분리에 있어서 물에 대한 선택성을 증가시킨다. 따라서, 본 연구에서는 기질인 폴리아크릴로니트릴막의 탈수능력을 향상시키기 위해 카르복시기를 함유한 아크릴산을 공증합시켰다. 아크릴산-아크릴로니트릴 공중합체는 emulsifier-free copolymerization법을 사용하여 합성하였다. 공중합체내의 카르복시기함량을 변화시키기 위해 아크릴산의 농도를 변화시키면서 제조하였으며, 고분자막은 용매로 디메틸포름아미드(DMF)를 사용하여 고분자용액을 제조한 후, 유리판에 캐스팅하여 제조하였다. 이들 막을 사용하여 물/아세트산 혼합물의 분리를 시행하였으며. 고분자막의 두께변화, 공급액중 아세트산의 조성변화 그리고 공급액의 온도변화 등이 분리성능에 미치는 영향을 검토하였다.
Dehydration of water/acetic acid mixture by pervaporation was carried out through the membranes prepared from poly(acrylic acid-co-acrylonitrile). Hydrophilic groups such as carboxylic group and sulfonic group generally improve selectivity toward water in separating organic/water mixture. Carboxylic group was introduced in this study to enhance the dehydration ability of the base polyacrylonitrile(PAN) membrane. Poly(acrylic acid-co-acylonitrile) was synthesized by using emulsifier-free polymerization varying acrylic acid concentration to change the contents of carboxylic group in the copolymer. Membrane was prepared by casting 25wt% copolymer solution in dimethylformamide(DMF) onto a glass plate. Using these membranes, dehydration of water/acetic acid mixture was carried out. Effects of membrane thickness, feed concentration of acetic acid and feed temperature on the selectivity and the flux of the membranes were investigated.
- Lee YM, Polym.(Korea), 13(1), 3 (1989)
- Streitwieser A, Heathcock CH, "Introduction to Organic Chemistry," 3rd ed., p. 863, Macmillan Publishers (1985)
- Huang RYM, Xu Y, Jin Y, Lipski C, Proceedings of the Second International Conference on Pervaporation Processes in the Chemical Industry, San Antonio, USA, 8-11, March 1987, Bakish Materials Corporation, New Jersey, 225-239 (1987)
- Huang RYM, Yeom CK, J. Membr. Sci., 58, 33 (1991)
- Miyoshi H, boddeker KW, Mattenbach K, Wenzlaff A, Membr. J., 13(2), 109 (1988)
- Nguyen TQ, Essamri A, Clememt R, Neel J, Makromol. Chem., 188, 1973 (1987)
- Yoshikawa M, Yokoshi T, Sanui K, Ogata N, Membr. J., 10(4), 247 (1985)
- Lee YM, Bourgeois D, Belfort G, J. Membr. Sci., 44, 161 (1989)
- Ohtsuka Y, Kawaguchi H, Sugi Y, J. Appl. Polym. Sci., 26, 1638 (1981)
- Sakota K, Okaya T, J. Appl. Polym. Sci., 20(11), 3133 (1976)
- Juang MS, Krieger IM, J. Polym. Sci. A: Polym. Chem., 14, 2089 (1976)
- Matsumoto T, Okubo M, Onoe S, Kobunshi Ronbunshu, 33(10), 565 (1976)
- Sagota K, Okaya T, J. Appl. Polym. Sci., 20(7), 1725 (1976)
- Sakota K, Okaya T, J. Appl. Polym. Sci., 20(7), 1745 (1976)
- Goodall AR, Wilkinson MC, Hearn J, J. Polym. Sci. A: Polym. Chem., 15, 2193 (1977)
- Kim JH, Kim KY, Polym.(Korea), 11(1), 71 (1987)
- Kesting, "Snthetic Polymeric Membranes," 2nd Ed., A Wiley-Interscience Publication, p. 159, New York (1985)
- Reichenberg D, Wall W, J. Chem. Soc., 3364 (1956)
- Aptel P, Challard N, Cuny J, Neel J, J. Membr. Sci., 1, 271 (1976)
- Lee YM, Wang WJ, Makromol. Chem., 191, 3131 (1990)
- Spitzen JWF, Ph.D. Thesis, Twente University, Netherlands, 28 (1988)
- Spitzen JWF, Koops GH, Mulder MHV, Smolders CA, Proceeding of 3rd International Conference on Pervaporation Process in the Chemical Industry, p. 252, Held in Nancy, France, Sept. 19-22 (1988)
- Lee YM, Won G, Polym. J., 22(7), 578 (1990)