Journal of the Korean Industrial and Engineering Chemistry, Vol.12, No.2, 212-217, April, 2001
고압에서 Poly(octadecyl methacrylate)-CO2 혼합물에 대한 상거동과 공용매의 효과
Cosolvent Effect and Phase Behavior of Poly(octadecyl methacrylate)-CO2 Mixtures at High Pressure
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초록
고압에서 이성분계 CO2-octadecyl methacrylate (ODMA) 혼합물에 대해 압력-조성의 상거동 실험을 온도 50, 80, 110 및 130 ℃와 압력 22∼337 bar 의 범위에서 행하였다. 일정 압력에서 CO2에 대한 ODMA의 용해도는 온도가 증가함에 따라 증가함을 보였다. CO2-ODMA계의 실험결과를 Peng-Robinson 상태방정식에서 적용하였고, 온도에 독립적인 피라미터를 이용하여 구한 계산값을 실험값과 비교하였다. 순수 CO2와 ODMA의 임계온도와 실험 온도 사이에서 압력변화에 따라 CO2-ODMA 계의 임계궤적(critical locus)을 얻었고, 임계온도 구간에서 곡선은 최대값을 나타내었다. 또한 초임계 이산화탄소-poly(octadecyl methacrylate) (PODMA) ODMA의 3성분 혼합물에 대해 온도 35∼254 ℃, 압력 1946 bar까지, 그리고 공용매 ODMA 농도 10.2, 23.2, 29.7, 39.3 및 49.7 wt%에서 상거동 자료들을 얻었다. 공용매의 농도 증가에 따라 위아래임계용해온도(U-LCST) 영역으로부터 아래임계용해온도(LCST) 영역까지의 상거동 곡선에서 압력-온도 기울기의 변화를 관찰하였다. PODMA-CO2 혼합물에 ODMA이 농도가 51.7 wt%일 때 삼상(LLV)이 나타났다. PODMA는 온도 255 ℃, 압력 2700 bar에서도 순수 CO2에 용해되지 않았다.
Pressure-composition isotherms were measured for the CO2-octadecyl methacrylate (ODMA) at 50, 80, 110 and 130 ℃ and at pressures from 22 to 337 bar. The solubility of ODMA in the CO2-ODMA mixture increased as the temperature increased at constant pressure. The experimental results for the CO2-ODMA mixture were correlated using Peng-Robinson equation of state with temperature-independent parameters. The experimental data were compared with the calculated data by the Peng-Robinson equation of state for the CO2-ODMA mixture. The CO2-ODMA mixture had continuous critical mixture curves that shows maximum pressures at temperatures between the critical temperatures of CO2 and ODMA. Phase behavior data for ternary poly(octadecyl methacrylate) (PODMA)-CO2-ODMA were measured in the temperature range from 35 to 254 ℃ and pressures up to 1946 bar. The cosolvent(ODMA) concentrations were 10.2, 23.2, 29.7, 39.3 and 49.7 wt%. The mixture changed the pressure-temperature slope of the phase behavior from U-LCST region to LCST region as the cosolvent concentration increased. The addition of 51.7 wt% ODMA to PODMA-CO2 mixture showed LLV phase behavior. The PODMA did not dissolve in pure CO2 even at 255 ℃and 2700 bar.
Keywords:Poly(octadecyl methacrylate)-CO2-octadecyl methacrylate system;Cosolvent effect;CO2-octadecyl methacrylate system;Phase behavior
- McHugh MA, Rindfleisch F, Kuntz PT, Schmaltz C, Buback M, Polymer, 39(24), 6049 (1998)
- DeSimone JM, Guan Z, Elsbernd CS, Science, 257, 945 (1992)
- Buback M, Droge T, Macromol. Chem. Phys., 200, 256 (1999)
- Canelas D, DeSimone JM, Adv. Polym. Sci., 133, 103 (1997)
- McHugh MA, Guckes TL, Macromolecules, 18, 674 (1985)
- Pan C, Radosz M, Ind. Eng. Chem. Res., 38(7), 2842 (1999)
- Kinzl M, Luft G, Adidharma H, Radosz M, Ind. Eng. Chem. Res., pending (1999)
- Kirby CF, McHugh MA, Chem. Rev., 99(2), 565 (1999)
- Wolf BA, Blaum G, J. Polym. Sci. B: Polym. Phys., 13, 1115 (1975)
- Wolf BA, Blaum G, Makromol. Chem., 177, 1073 (1976)
- Chen AQ, Radosz M, J. Chem. Eng. Data, 44, 854 (1999)
- Lora M, McHugh MA, Fluid Phase Equilib., 157(2), 285 (1999)
- Rindfleisch F, DiNoia TP, McHugh MA, J. Phys. Chem., 100(38), 15581 (1996)
- Kim K, Byun HS, HWAHAK KONGHAK, 38(4), 479 (2000)
- Byun HS, McHugh MA, Ind. Eng. Chem. Res., 39(12), 4658 (2000)
- Byun HS, Jeon NS, Fluid Phase Equilib., 167(1), 113 (2000)
- Byun HS, Kim K, McHugh MA, Ind. Eng. Chem. Res., 39(12), 4580 (2000)
- Reid RC, Prausnitz JM, Polling BE, "The Properties of Gases and Liquids", 4th ed., McGraw-Hill, New York (1987)
- Vargaftik NB, "Handbook of Physical Properties of Liquid and Gases" Springer-Verlag, Berlin (1983)
- Lee BI, Kesler MG, AIChE J., 21, 510 (1975)
- Peng DY, Robinson DB, Ind. Eng. Chem. Res. Fundam., 15, 59 (1976)
- McHugh MA, Krukonis VJ, "Supercritical Fluid Extraction: Principles and Practice", 2nd ed., Stoneham, Butterworth, MA (1994)
- Scott RL, Konynenburg PB, Discuss. Faraday Soc., 49, 87 (1970)
- Hasch BM, Maurer EJ, Ansanelli LF, McHugh MA, J. Chem. Thermodyn., 26(6), 625 (1994)
- Schneider GM, Adv. Chem. Phys., 17, 1 (1970)
- Byun HS, Choi TH, J. Korean Ind. Eng. Chem., 11(4), 396 (2000)