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Received May 9, 2013
Accepted August 18, 2013
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Effects of sweating time and cooling strategy on purification of N-vinyl-2-pyrrolidinone using a melt crystallizer
Department of Chemical and Biological Engineering, Korea University, Seoul 136-701, Korea 1Department of Chemical Engineering, Kyung Hee University, Suwon 449-701, Korea
jwkang@korea.ac.kr
Korean Journal of Chemical Engineering, November 2013, 30(11), 1997-2000(4), 10.1007/s11814-013-0158-9
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Abstract
A melt crystallization process is proposed to produce high-purity n-vinyl-2-pyrrolidinone (NVP). To produce high purity products, operation strategy plays key role in the melt crystallizer. We investigated the cooling strategy and optimal sweating time using a batch-type melt crystallizer. A slow cooling followed by a slow heating was found to be an effective temperature profile to produce high purity of NVP. The optimal sweating time was found to be about 20 minutes. For industrial application, a cascade melt crystallizer which consists of four stages was constructed and the proposed crystallization/sweating scheme was applied. Using the new melt crystallizer, NVP more than 99.99% purity can be produced in semi-continuous mode.
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References
Harreus AL, 2-Pyrrolidone, In: Gerhartz W, Yamamoto YS, Ullmann’s Encyclopedia of Chemical Technology, 5th Ed., Deerfield Beach, FL, VCH Publishers (1993)
Chowdhury J, Chem. Eng., 24 (1988)
Genck WJ, Chem. Process., 63 (1988)
McCallion J, Chem. Process., 33 (1989)
Rittner S, Steiner R, Chem. Ing. Technol., 57, 91 (1985)
Wynn N, Chem. Eng., 26 (1986)
Gilbert SW, AIChE J., 37, 1205 (1991)
Kim KJ, Ulrich J, J. Colloid Interface Sci., 252(1), 161 (2002)
Matsuoka M, Ohishi M, Kasama S, J. Chem. Eng. Japan., 19, 181 (1986)
Matsuoka M, Fukuda T, Takagi Y, Takiyama H, J. Cryst.Growth., 166, 1035 (1996)
Kim KJ, Ulrich J, J. Cryst. Growth, 234(2-3), 551 (2002)
Jancic SJ, Sulzer Technical Review, Sulzer Brothers Limited, Winterthur, Switzerland (1986)
Papp A, Saxer K, Verfahrenstechnik., 15, 195 (1981)
Chem. Eng. Prog., 64 (1980)
Chowdhury J, Chem. Eng., 24 (1988)
Genck WJ, Chem. Process., 63 (1988)
McCallion J, Chem. Process., 33 (1989)
Rittner S, Steiner R, Chem. Ing. Technol., 57, 91 (1985)
Wynn N, Chem. Eng., 26 (1986)
Gilbert SW, AIChE J., 37, 1205 (1991)
Kim KJ, Ulrich J, J. Colloid Interface Sci., 252(1), 161 (2002)
Matsuoka M, Ohishi M, Kasama S, J. Chem. Eng. Japan., 19, 181 (1986)
Matsuoka M, Fukuda T, Takagi Y, Takiyama H, J. Cryst.Growth., 166, 1035 (1996)
Kim KJ, Ulrich J, J. Cryst. Growth, 234(2-3), 551 (2002)
Jancic SJ, Sulzer Technical Review, Sulzer Brothers Limited, Winterthur, Switzerland (1986)
Papp A, Saxer K, Verfahrenstechnik., 15, 195 (1981)
Chem. Eng. Prog., 64 (1980)