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Molecular Simulation of Multicomponent Reaction and Phase Equilibria in MTBE Ternayr System

机译:MTBE Ternayr系统中多组分反应和相平衡的分子模拟

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摘要

Reaction and phase equilibria in the isobutene + methanol + MTBE ternary system were studied using the reaction-ensemble Monte Carlo (REMC) simulation method. The S)'stem was modeled at the molecular level by an OPLS force field. No adjustable binal)'cross-interaction parame,ersor mixture data ofany kind were used in the simula- tion model, ilnd only vapor-pl'essure data for the pure components was required as input. The REMCmethod alsoconJPutes excess internal energies and molar volumes as a biproduct of the simulations. Both the nonreacting and reacting ternary S)'stems were considered over the temperature range of practical interest at 5 bar. Results are com- pared with the calculations using twq conventional thermodynamic approaches: the Wilson andUNIFAC free-enelRY 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 thel':'Jodynamic approaches, and they are alguably more accurate.
机译:利用反应谱法蒙特卡洛(REMC)模拟方法研究了异丁烯+甲醇+ MTBE三元体系中的反应和相平衡。通过OPLS力场在分子水平上模拟了S)的茎。在模拟模型中,没有使用任何可调节的二元交联参数,也没有使用任何种类的混合气体或混合数据,并且仅需要纯组分的蒸气压数据作为输入。 REMC方法还将多余的内部能量和摩尔体积作为模拟的副产品进行计算。在5巴的实际应用温度范围内,均考虑了非反应性和反应性三元醇的反应。将结果与使用第二种常规热力学方法进行的计算进行比较:Wilson和UNIFAC液相自由烯键模型。在这两种情况下,气相的状态方程均被截断。计算机仿真结果与“动态”方法相似,并且可以说更准确。

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