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首页> 外文期刊>Molecular simulation >The Extrapolation of Vapour-liquid Equilibrium Curves of Pure Fluids in Alternative Gibbs Ensemble Monte Carlo Implementations
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The Extrapolation of Vapour-liquid Equilibrium Curves of Pure Fluids in Alternative Gibbs Ensemble Monte Carlo Implementations

机译:替代Gibbs集合蒙特卡罗实现中纯流体的汽-液平衡曲线的外推

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Extrapolation schemes based on Taylor series expansion to determine the vapour-liquid equilibrium (VLE) curves of pure molecular fluids are presented for the NpH and μVL versions of the Gibbs ensemble Monte Carlo (GEMC) simulations. The coexistence curves of the various configurational quantities can be expressed as Taylor series around the simulated equilibrium point as a function of pressure in the NpH version and chemical potential in the μVL version. The coefficients of the Taylor series are calculated from single GEMC simulations using Clapeyron-like equations and fluctuation formulas. A Pade approximant is used to widen the range where the extrapolation is accurate. These methods are demonstrated on atomic Lennard-Jones fluid. The procedure is found to be an accurate and useful tool to calculate wide sections of the VLE curves. With this procedure the saturation heat capacity can be directly determined using the calculated derivatives.
机译:提出了基于泰勒级数展开来确定纯分子流体的汽液平衡(VLE)曲线的外推方案,用于吉布斯合奏蒙特卡洛(GEMC)模拟的NpH和μVL版本。各种构型量的共存曲线可以表示为模拟平衡点周围的泰勒级数,该值是NpH版本中压力和μVL版本中化学势的函数。泰勒级数的系数是使用类似于克拉珀龙方程和涨落公式的单个GEMC模拟计算得出的。 Pade近似值用于扩大精确外推的范围。这些方法在原子Lennard-Jones流体上得到了证明。发现该程序是计算VLE曲线的宽截面的准确而有用的工具。通过此程序,可以使用计算出的导数直接确定饱和热容量。

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