Cao M, Monson P A
Department of Chemical Engineering, University of Massachusetts, Amherst, Massachusetts 01003, USA.
J Chem Phys. 2004 Feb 8;120(6):2980-8. doi: 10.1063/1.1637332.
Solid-fluid and solid-solid phase equilibrium for binary mixtures of hard sphere chains modeling n-hexane, n-heptane, and n-octane has been calculated using Monte Carlo computer simulations. Thermodynamic integration was used to calculate the Gibbs free energy and chemical potentials in the solid and fluid phases from pure component reference values. A multiple stage free energy perturbation method was used to calculate the composition derivative of the Gibbs free energy. Equation of state and free energy data for the fluid phase indicate ideal solution behavior. Nonideality is much more significant in the solid phase with only partial solubility of shorter chains in the longer chains and essentially no solubility at the other end of the composition range. The miscibility decreases with increasing chain length difference between the components. For the model of n-hexane/n-octane mixtures solid--solid phase separation has been observed directly in some of the simulations, with the components segregating between the layers of the solid structure. The behavior is similar to that seen in some binary n-alkane mixtures with longer chain lengths but comparable chain length ratios between the components. Such phase separation, although indicated thermodynamically, is not seen directly in the simulations of the n-heptane/n-octane mixture due to the difference in the pure component crystal structures.
使用蒙特卡罗计算机模拟计算了模拟正己烷、正庚烷和正辛烷的硬球链二元混合物的固-液和固-固相平衡。采用热力学积分从纯组分参考值计算固液两相中的吉布斯自由能和化学势。使用多阶段自由能微扰法计算吉布斯自由能的组成导数。流体相的状态方程和自由能数据表明其具有理想溶液行为。非理想性在固相中更为显著,较短链在较长链中只有部分溶解度,而在组成范围的另一端基本没有溶解度。随着组分之间链长差异的增加,混溶性降低。对于正己烷/正辛烷混合物模型,在一些模拟中直接观察到了固-固相分离,组分在固体结构的层间分离。这种行为与一些链长较长但组分之间链长比相当的二元正构烷烃混合物中观察到的行为相似。尽管从热力学上表明了这种相分离,但由于纯组分晶体结构的差异,在正庚烷/正辛烷混合物的模拟中并未直接观察到。