Korean Journal of Chemical Engineering, Vol.32, No.5, 958-966, May, 2015
Phase behavior for the poly(2-methoxyethyl acrylate)+supercritical solvent+cosolvent mixture and CO2+2-methoxyethyl acrylate system at high pressure
E-mail:
High pressures phase equilibrium data were presented for the CO2+2-MEA system at temperatures ranging from (313.2 to 393.2) K and pressures up to ca. 17.97MPa. The CO2+2-MEA system exhibited type-I phase behavior and was modeled using the Peng-Robinson equation of state. The phase behavior data were reported for poly(2-methoxyethyl acrylate) [P(2-MEA)] in supercritical CO2 and dimethyl ether (DME), as well as for the P(2-MEA)+2-methoxyethyl acrylate (2-MEA) (or DME) in CO2. The cloud-point data were measured for the P(2-MEA)+DME in supercritical CO2 at temperature range of (333-453) K and a pressure range of (8.79-199.14) MPa. The P(2-MEA) in supercritical CO2 was soluble to 453 K and pressure of 199MPa. The phase behavior for the P(2-MEA)+CO2+2-MEA mixture was measured in changes of the pressure-temperature (p, T) slope and with 2-MEA mass fraction of 0.0 wt%, 8.4 wt%, 17.1 wt%, 45.4 wt% and 65.0wt%. With 74.5 wt% 2-MEA to the P(2-MEA)+CO2 solution, the cloud-point
curves took on the appearance of a typical lower critical solution temperature boundary, liquid+liquid transition and liquid+vapor transition. The location of the P(2-MEA)+CO2 cloud-point curve shifted to lower temperatures and pressures upon the addition of 2-MEA or DME.
Keywords:Poly(2-Methoxyethyl Acrylate);2-Methoxyethyl Acrylate;High Pressure Phase Behavior;Cloud-point Pressures;Supercritical CO2;Dimethyl Ether
- Jessop PG, Hsiao Y, Ikariya T, Noyori R, J. Am. Chem. Soc., 118(2), 344 (1996)
- Beckman EJ, J. Supercrit. Fluids, 28(2-3), 121 (2004)
- Kikic I, Vecchione F, Curr. Opin. Solid State Mater. Sci., 7, 399 (2003)
- Kazarian SG, Supercritical fluid technology for drug product development, chapter Supercritical Fluid Impregnation of Polymers for Drug Delivery, Marcel-Dekker, 343 (2004)
- Reverchon E, Cardea S, J. Membr. Sci., 240(1-2), 187 (2004)
- Shieh YT, Liu KH, J. Polym. Sci. B: Polym. Phys., 42(13), 2479 (2004)
- Baldyga J, Henczka M, Shekunov BY, Drugs Pharm. Sci., 138, 91 (2004)
- Mueller XM, Jegger D, Augstburger M, Horisberger J, von Segesser LK, Int. J. Artif. organs, 25, 223 (2002)
- Tanaka M, Motomura K, Ishii N, Shimura K, Onishi M, Mochizuki A, Hatakeyama T, Polym. Int., 49, 1709 (2000)
- Tanaka M, Mochizuki A, Shiroya T, Motomura K, Shimura M, Onishi M, Okahaba Y, Colloids Surf., A, 203, 195 (2002)
- Tanaka M, Mochizuki A, Motomura K, Shimura M, Onishi M, Okahata Y, Colloids Surf., A, 193, 145 (2001)
- Tanaka M, Bio-Med. Mater. Eng., 14, 427 (2004)
- Tanaka M, Mochizuki A, J. Biomed. Mater. Res. A, 68, 684 (2003)
- Tanaka M, Blood compatibility of poly(2-methoxyethyl acrylate): Design of a novel bio-interface, Ph. Dissertation D, Hokkaido University, Sapporo, Hokkaido (2003)
- Wang B, He J, Sun DH, Zhang R, Han BX, Fluid Phase Equilib., 239(1), 63 (2006)
- Byun HS, Choi TH, Korean J. Chem. Eng., 21(5), 1032 (2004)
- Kim SH, Jang YS, Yoon SD, Byun HS, Fluid Phase Equilib., 312, 93 (2011)
- Yoon SD, Kim CR, Byun HS, Fluid Phase Equilib., 365, 97 (2014)
- Yoon SD, Byun HS, Korean J. Chem. Eng., 31(3), 522 (2014)
- Cho SH, Yang DS, Byun HS, Fluid Phase Equilib., 351, 18 (2013)
- Fornari RE, Alessi P, Kikic I, Fluid Phase Equilib., 57, 1 (1990)
- Dohrn R, Brunner G, Fluid Phase Equilib., 106(1-2), 213 (1995)
- Christov M, Dohrn R, Fluid Phase Equilib., 202(1), 153 (2002)
- Dohrn R, Peper S, Fonseca JMS, Fluid Phase Equilib., 288(1-2), 1 (2010)
- Fonseca JMS, Dohrn R, Peper S, Fluid Phase Equilib., 300(1-2), 1 (2011)
- McHugh MA, Rindfleisch F, Kuntz PT, Schmaltz C, Buback M, Polymer, 39(24), 6049 (1998)
- Rindfleisch F, DiNoia TP, McHugh MA, J. Phys. Chem., 100(38), 15581 (1996)
- Jang YS, Byun HS, J. Chem. Eng. Data, 59(5), 1391 (2014)
- Poling BE, Prausnitz JM, O’Connell JP, The Properties of Gases and Liquid, 5th Ed., McGraw-Hill, New York (2001)
- Yang DS, Cho SH, Yoon SD, Jeong HH, Byun HS, J. Supercrit. Fluids, 79, 11 (2013)
- Cho SH, Yoon SD, Byun HS, Korean J. Chem. Eng., 30(3), 739 (2013)
- Yoon SD, Byun HS, J. Chem. Thermodyn., 71, 91 (2014)
- Chirico RD, Frenkel M, Diky VV, Marsh KN, Wilhoit RC, J. Chem. Eng. Data, 48(5), 1344 (2003)
- Scott RL, van Konynenburg PB, Discuss. Faraday Soc., 49, 87 (1970)
- McHugh MA, Krukonis VJ, Supercritical fluid extraction: Principles and practice, Butterworth, Boston, MA (1994)
- Peng DY, Robinson DB, Ind. Eng. Chem. Res. Fundam., 15, 59 (1976)
- http://www.chemspider.com/chemical-structure.17368.html.
- Albrecht KL, Stein FP, Han SJ, Gregg CJ, Radosz M, Fluid Phase Equilib., 117(1-2), 84 (1996)
- Tsang CY, Streett WB, J. Chem. Eng. Data, 26, 155 (1981)
- Wolf BA, Blaum GJ, J. Polym. Sci., Polym. Phys. Ed., 13, 1115 (1975)
- Patterson D, Pure Appl. Chem., 31, 133 (1972)