Molecular simulation of multicomponent reaction and phase equilibria in MTBE ternary system
- 16 April 2000
- journal article
- thermodynamics
- Published by Wiley in AIChE Journal
- Vol. 46 (4), 866-875
- https://doi.org/10.1002/aic.690460419
Abstract
Reaction and phase equilibria in the isobutene + methanol + MTBE ternary system were studied using the reaction‐ensemble Monte Carlo (REMC) simulation method. The system was modeled at the molecular level by an OPLS force field. No adjustable binary cross‐interaction parameters or mixture data of any kind were used in the simulation model, and only vapor‐pressure data for the pure components was required as input. The REMC method also computes excess internal energies and molar volumes as a biproduct of the simulations. Both the nonreacting and reacting ternary systems were considered over the temperature range of practical interest at 5 bar. Results are compared with the calculations using two conventional thermodynamic approaches: the Wilson and UNIFAC free‐energy models for the liquid phase, together with a truncated virial equation of state for the gas phase in both cases. Computer simulation results were similar to those of the thermodynamic approaches, and they are arguably more accurate.This publication has 16 references indexed in Scilit:
- Accurate Computer Simulation of Phase Equilibrium for Complex Fluid Mixtures. Application to Binaries Involving Isobutene, Methanol, Methyl tert-Butyl Ether, and n-ButaneThe Journal of Physical Chemistry B, 1999
- The reaction ensemble method for the computer simulation of chemical and phase equilibria. II. The Br2+Cl2+BrCl systemThe Journal of Chemical Physics, 1999
- Review of thermophysical property measurements on mixtures containing MTBE, TAME, and other ethers with non-polar solventsFluid Phase Equilibria, 1999
- The Use of Control Quantities in Computer Simulation Experiments: Application to the Exp-6 Potential FluidMolecular Simulation, 1995
- Monte Carlo simulation of liquid acetone with a polarizable molecular modelMolecular Physics, 1995
- Multiple solutions in reactive distillation for methyl tert-butyl ether synthesisIndustrial & Engineering Chemistry Research, 1993
- Direct Determination of Fluid Phase Equilibria by Simulation in the Gibbs Ensemble: A ReviewMolecular Simulation, 1992
- The influence of equilibrium chemical reactions on vapor—liquid phase diagramsChemical Engineering Science, 1988
- Phase equilibria by simulation in the Gibbs ensembleMolecular Physics, 1988
- Equilibrium constant for the methyl tert-butyl ether liquid-phase synthesis using UNIFACIndustrial & Engineering Chemistry Fundamentals, 1983