화학공학소재연구정보센터
Journal of Industrial and Engineering Chemistry, Vol.18, No.1, 414-419, January, 2012
Phase equilibria for the binary mixture of n-vinyl pyrrolidone and N,N-dimethylacrylamide in supercritical carbon dioxide
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High pressure phase equilibria for the (carbon dioxide + n-vinyl pyrrolidone) and (carbon dioxide + N,N-dimethylacrylamide) systems are measured in a static apparatus at five temperatures of 313.2, 333.2, 353.2, 373.2 and 393.2 K and pressures up to 24.66 MPa. These two systems exhibit maximums in pressure at temperatures between the critical temperatures of carbon dioxide and n-vinyl pyrrolidone or N,N-dimethylacrylamide. The solubility of n-vinyl pyrrolidone and N,N-dimethylacrylamide for the carbon dioxide + n-vinyl pyrrolidone and carbon dioxide + N,N-dimethylacrylamide systems increases as the temperature increases at a fixed pressure. The carbon dioxide + n-vinyl pyrrolidone and carbon dioxide + N,N-dimethylacrylamide systems exhibit type-I phase behavior. The experimental results for the carbon dioxide + n-vinyl pyrrolidone and carbon dioxide + N,N-dimethylacrylamide systems are correlated with the Peng.Robinson equation of state using a mixing rule including binary interaction parameters (kij and ηij).
  1. Pratt JA, McHugh MA, J. Supercrit. Fluids, 9(1), 61 (1996)
  2. Cooper AI, J. Mater. Chem., 10, 207 (2000)
  3. Desimone JM, Maury EE, Menceloglu YZ, Mcclain JB, Romack TJ, Combes JR, Science, 265(5170), 356 (1994)
  4. Byun HS, Choi MY, Lim JS, J. Supercrit. Fluids, 37(3), 323 (2006)
  5. Byun HS, Lee HY, J. Chem. Eng. Data., 51, 1436 (2006)
  6. http://www.inventec.dehon.com.
  7. Bae W, Kwon SY, Byun HS, Kim HY, J. Supercrit. Fluids, 30(2), 127 (2004)
  8. Santos WLF, Favareto R, Cabral VF, Muniz EC, Cardozo L, Rubira AF, J. Supercrit. Fluids, 38(3), 319 (2006)
  9. Byun HS, Kim NH, Kwak C, Fluid Phase Equilib., 208(1-2), 53 (2003)
  10. Peng DY, Robinson DB, Ind. Eng. Chem. Fundam., 15, 59 (1976)
  11. Poling BE, Prausnit JM, O’Connell JP, The Properties of Liquids and Gases, 5thed., McGraw-Hill, New York (2001)
  12. Byun HS, Lee DH, Ind. Chem. Eng. Res., 45, 3354 (2006)
  13. Byun HS, Hasch BM, McHugh MA, Fluid Phase Equilib., 115(1-2), 179 (1996)
  14. Kuester JL, Mize JH, Optimization Techniques with Fortran, McGraw-Hill, New York (1973)
  15. http://www.chemnet.com/dict/dict-2680-03-7.kr.html.
  16. McHugh MA, Krukonis VJ, Supercritical Fluid Extraction, 2nd ed., Butterworth-Heinemann, Stoneham (1994)
  17. Scott RL, Van Kontnenburg PB, Discuss. Faraday Soc., 49, 87 (1970)