LLE of Solvent-Water-2-Propanol Ternary Systems

Solvent-water-2-propanol 삼성분계의 액-액평형

  • Jeong, Sang-Hoon (Dept. of Chem. Eng., College of Eng., Dong-A Univ.) ;
  • Lee, Jin-Woo (Dept. of Chemical Industry, Dong-Eui Technical Junior College) ;
  • Park, Dong-Won (Dept. of Chem. Eng., College of Eng., Dong-A Univ.)
  • 정상훈 (동아대학교 공과대학 화학공학과) ;
  • 이진우 (동의공업전문대학 화학공업과) ;
  • 박동원 (동아대학교 공과대학 화학공학과)
  • Received : 1997.04.21
  • Accepted : 1997.05.30
  • Published : 1997.08.10

Abstract

Due to the rising cost of energy, new separation processes based on extraction are becoming more attractive than before. Thus, the need for calculating and predicting liquid-liquid equilibria(LLE) compositions has very much increased. The purpose of this study is to determine the binodal curves, tie line, plait point, distribution and selectivity for the ternary systems of 2-propanol-water with methyl ethyl ketone, methyl isobutyl ketone, ethylacetate, toluene and o-xylene as solvents at $25^{\circ}C$. And those tie line data were used to examine thermodynamic consistency. The experimental tie line data were correlated with NRTL and UNIQUAC models.

에너지 비용의 상승에 따라 추출의 기본원리를 둔 새로운 분리공정에 대한 연구가 많이 진행되고 있으며, 이에 따라 액-액평형 조성의 계산 및 예측에 대한 필요성이 매우 증가하고 있다. 본 연구에서는 공비혼합물을 형성하는 2-propanol 수용액에 용매로서 methyl ethyl ketone, methyl isobutyl ketone, ethylacetate, butylacetate, toluene 및 o-xylene을 첨가한 삼성분계에 대하여 $25^{\circ}C$에서 용해도곡선, tie line, plait point, 분배계수와 선택도를 실험을 통해 구하였다. Tie line 데이터의열역학적 건전성을 확인하였으며 실험값을 NRTL 및 UNIQUAC 모델식으로 구한 계산값과 비교하였다.

Keywords

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