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Received February 7, 2004
Accepted April 20, 2004
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Solubility in the Binary and Ternary System for Poly(alkyl acrylate)-Supercritical Solvent Mixtures
Department of Chemical Engineering, Yosu National University, Yosu, Chonnam 550-749, Korea
Korean Journal of Chemical Engineering, July 2004, 21(4), 874-881(8), 10.1007/BF02705533
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Abstract
Experimental cloud-point data to 210 ℃ and 2,200 bar are presented for binary and ternary mixtures of poly(methyl acrylate)-CO2-methy acrylate and poly(ethyl acrylate)-CO2, propylene, and 1-butene-ethyl acrylate systems. The accuracy of the experimental apparatus was tested by comparing the measured pressure-temperature phase behavior data of the poly(ethyl acrylate)-CO2 system obtained in this study with those of Rindfleisch et al. [1995]. The phase behaviors for the system poly(methyl acrylate)-CO2-methyl acrylate were measured in changes of pressure-temperature slope, and with cosolvent concentrations of 0, 5.0, 13.7, 25.3, and 43.3 wt%, respectively. With 48.3 wt% methyl acrylate to the poly(methyl acrylate)-CO2 solution significantly changes, the phase behavior curve takes on the appearance of a typical lower critical solution temperature (LCST) boundary. The impact of ethyl acrylate on the cloudpoint for the poly(ethyl acrylate)-CO2 system shows the change of slope of the phase behavior curves from negative to positive with ethyl acrylate concentration of 0, 8.2, and 25.0 wt%. The cloud-point behavior for the poly(ethyl acrylate)-CO2-39.5 wt% ethyl acrylate system shows an LCST curve. The solubility curve to ~150 ℃ and 1,650 bar for poly(ethyl acrylate)-propylene-ethyl acrylate system shows the change of pressure-temperature diagram and with ethyl acrylate concentration of 0, 7.2 and 21.0 wt%. Also, when 41.1 wt% ethyl acrylate was added to the poly(ethyl acrylate)-propylene solution, the phase behavior curve showed the LCST region. The high pressure phase behavior of poly(ethyl acrylate)-1-butene-0, 3.1, 8.1, 18.5 and 30.7 wt% ethyl acrylate system presented the change of pressuretemperature curve from the UCST region to U-LCST region as the ethyl acrylate concentration increased.
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References
Byun HS, Choi TH, J. Appl. Polym. Sci., 86(2), 372 (2002)
Byun HS, Lee HY, HWAHAK KONGHAK, 40(6), 703 (2002)
Byun HS, McHugh MA, Ind. Eng. Chem. Res., 39(12), 4658 (2000)
Byun HS, Park C, Korean J. Chem. Eng., 19(1), 126 (2002)
Christian P, Giles MR, Griffiths RMT, Irvine DJ, Major RC, Howdle SM, Macromolecules, 33(25), 9222 (2000)
Conway SE, Byun HS, McHugh MA, Wang JD, Mandel FS, J. Appl. Polym. Sci., 80(8), 1155 (2001)
DeSimone JM, Zihibin G, Elsebernd CS, Science, 257, 945 (1992)
Kajimoto O, Proceeding of the 8th Meeting on Supercritical Fluids, France, pp. 31-40 (2002)
Kiran E, Liu K, Korean J. Chem. Eng., 19(1), 153 (2002)
Kirby CF, McHugh MA, Chem. Rev., 99(2), 565 (1999)
Lee BC, Kim NI, Korean J. Chem. Eng., 19(1), 132 (2002)
Lee SH, McHugh MA, Korean J. Chem. Eng., 19(1), 114 (2002)
McHugh MA, Krukonis VJ, "Supercritical Fluid Extraction: Principles and Practice," 2nd ed., Butterworths Publishers, Stoneham, MA (1993)
McHugh MA, Rindfleisch F, Kuntz PT, Schmaltz C, Buback M, Polymer, 39(24), 6049 (1998)
Mertdogan CA, McHugh MA, Barth HG, Walls DJ, Tuminello WH, Int. J. Polym. Anal. Characterization, 4, 231 (1997)
Patterson D, Polym. Eng. Sci., 22, 64 (1982)
Pratt JA, McHugh MA, J. Supercrit. Fluids, 9(1), 61 (1996)
Rindfleisch F, DiNoia TP, McHugh MA, J. Phys. Chem., 100(38), 15581 (1996)
Shiho H, DeSimone J, Macromolecules, 34(5), 1198 (2001)
Wolf BA, Blaum G, J. Polym. Sci. B: Polym. Phys., 13, 1115 (1975)
Byun HS, Lee HY, HWAHAK KONGHAK, 40(6), 703 (2002)
Byun HS, McHugh MA, Ind. Eng. Chem. Res., 39(12), 4658 (2000)
Byun HS, Park C, Korean J. Chem. Eng., 19(1), 126 (2002)
Christian P, Giles MR, Griffiths RMT, Irvine DJ, Major RC, Howdle SM, Macromolecules, 33(25), 9222 (2000)
Conway SE, Byun HS, McHugh MA, Wang JD, Mandel FS, J. Appl. Polym. Sci., 80(8), 1155 (2001)
DeSimone JM, Zihibin G, Elsebernd CS, Science, 257, 945 (1992)
Kajimoto O, Proceeding of the 8th Meeting on Supercritical Fluids, France, pp. 31-40 (2002)
Kiran E, Liu K, Korean J. Chem. Eng., 19(1), 153 (2002)
Kirby CF, McHugh MA, Chem. Rev., 99(2), 565 (1999)
Lee BC, Kim NI, Korean J. Chem. Eng., 19(1), 132 (2002)
Lee SH, McHugh MA, Korean J. Chem. Eng., 19(1), 114 (2002)
McHugh MA, Krukonis VJ, "Supercritical Fluid Extraction: Principles and Practice," 2nd ed., Butterworths Publishers, Stoneham, MA (1993)
McHugh MA, Rindfleisch F, Kuntz PT, Schmaltz C, Buback M, Polymer, 39(24), 6049 (1998)
Mertdogan CA, McHugh MA, Barth HG, Walls DJ, Tuminello WH, Int. J. Polym. Anal. Characterization, 4, 231 (1997)
Patterson D, Polym. Eng. Sci., 22, 64 (1982)
Pratt JA, McHugh MA, J. Supercrit. Fluids, 9(1), 61 (1996)
Rindfleisch F, DiNoia TP, McHugh MA, J. Phys. Chem., 100(38), 15581 (1996)
Shiho H, DeSimone J, Macromolecules, 34(5), 1198 (2001)
Wolf BA, Blaum G, J. Polym. Sci. B: Polym. Phys., 13, 1115 (1975)