| Issue |
Korean Chemical Engineering Research,
Vol.57, No.1, 73-77, 2019
Vol.57, No.1, 73-77, 2019
Phase Equilibrium of Binary Mixture for the (propylene oxide + 1-pentanol) System at Several Temperatures
Isothermal (vapor + liquid) equilibrium data measurements were undertaken for the binary mixtures of (propylene oxide + 1-pentanol) system at three different temperatures (303.15, 318.15, and 333.15) K. The Peng-Robinson- Stryjek-Vera equation of state (PRSV EOS) was used to correlate the experimental data. The van der Waals onefluid mixing rule was used for the vapor phase and the Wong-Sandler mixing rule, which incorporates the non-random two liquid (NRTL) model, the universal quasi-chemical (UNIQUAC) model and the Wilson model, was used for the liquid phase. The experimental data were in good agreement with the correlation results.
[References]
- Russo V, Tesser R, Santacesaria E, Di Serio M, Ind. Eng. Chem. Res., 52(3), 1168, 2013
- Zhang WY, Wang H, Wei W, Sun YH, J. Mol. Catal. A-Chem., 231(1-2), 83, 2005
- Kim H, Hyeong S, Hong JH, Kim AR, Shin MS, Kim H, J. Chem. Thermodyn., 86, 1, 2015
- Stryjek R, Vera JH, Can. J. Chem. Eng., 64, 323, 1986
- Wong DSH, Sandler SI, AIChE J., 38, 671, 1992
- Renon H, Prausnitz JM, AIChE J., 14, 135, 1968
- Abrams DS, Prausnitz JM, AIChE J., 21, 116, 1975
- Wilson GM, J. Am. Chem. Soc., 86, 127, 1964
- “Guidelines for Evaluating and Expressing the Uncertainty of NIST Measurement Results,” NIST Technical Note 1297, 1994 Edition.
- Horstmann S, Gardeler H, Fischer K, Koster F, Gmehling J, J. Chem. Eng. Data, 46, 337, 2001
- NIST Chemistry Webbook Home Page. http://webbook.nist.gov/chemistry/(accessed Oct 15, 2018).
- DIPPR 801 Database, Design Institute for Physical Property Data, American Institute of Chemical Engineers (2002).
참고문헌정보(참고문헌, 인용문헌)는 화학공학소재연구정보센터에 의해 제공되고 있습니다.