摘要本文介绍了国内外α -烯烃的需求量和生产技术 ,以及我国目前α-烯烃的生产能力和状况。It introduces production technique and demand of α-alkene hydrocarbon at home and abroad,and its production capacity and status in our country present.
2Weidlich U, Gmehling J. A Modified U NIFAC Model 1: Prediction of VLE,h^E and γ^∞ [J]. Ind Eng Chem Res, 1987,26: 1372- 1381.
3Gmehling J, Li J,Schiller M. A Modified UNIFAC Model 2: Present Parameter Matrix and Results for Different Thermodynamic Properties[J]. Ind Eng Chem Res, 1993,32 : 178-193.
4Diamond D, Hahn T,Becker H et al. Improving the Understanding of a Novel Complex Azeotropic Distillation Process Using a Simplified Graphical Model and Simulation[J]. Chemical Engineering and Processing, 2004,43:483-493.
5Gross J, Sadowski G. Perturbed-Chain SAFT: an equation of state bades on a perturbation theory for chain molecules. Ind. Eng. Chem. Res, 2001, 40: 1244-1260.
6Huang S H, Radosz M. Equation of state for small, large, polydisperse, and associating molecules: extensions to fluid mixtures. Ind. Eng. Chem. Res. , 1991, 30:1994-2005.
7Dahl S, Michelsen M L. High-pressure vapor-liquid equilibrium with a UNIFAC-based equation-of-state. AIChEJ., 1990, 36:1829-1836.
8Wong D S, Sandier S I. A theoretically correct new mixing rule for cubic equations oil state ifor both highly and slightly non-ideal mixtures. AIChEJ., 1992, 38:671-680.
9Holderbaum T, Gmehling J. RKS-HG: group contribution equation-of-state based on UNIFAC. Fluid Phase Equilibria, 1991, 70:251-265.
10Edward K L, Davlson R R. Vapor-liquid equilibriums for the binary systems n-hexane with 2-methylpentane, 3- metbylpentane, and 2,4-dimethylpentane. Chem. Eng. Data, 1981, 26:85-88.
