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Mass and Heat Diffusion in Ternary Polymer Solutions: A Classical Irreversible Thermodynamics Approach

机译:三元聚合物溶液中的质量和热扩散:经典   不可逆热力学方法

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摘要

Governing equations for evolution of concentration and temperature inthree-component systems were derived in the framework of classical irreversiblethermodynamics using Onsager variational principle and were presented forsolvent/solvent/polymer and solvent/polymer/polymer systems. The derivation wasdeveloped from the Gibbs equation of equilibrium thermodynamics using the localequilibrium hypothesis, Onsager reciprocal relations and Prigogine theorem forsystems in mechanical equilibrium. It was shown that the details of mass andheat diffusion phenomena in a ternary system are completely expressed by a 3x3matrix whose entries are mass diffusion coefficients (4 entries), thermaldiffusion coefficients (2 entries) and three entries that describe theevolution of heat in the system. The entries of the diffusion matrix arerelated to the elements of Onsager matrix that are bounded by some constraintsto satisfy the positive definiteness of entropy production in the system. Allthe elements of diffusion matrix were expressed in terms of derivatives ofexchange chemical potentials of the components with respect to concentrationand temperature. The spinodal curves of ternary polymer solutions were derivedfrom the governing equations and their correctness was checked by the Hessianof free energy density. Moreover, it was proved that setting cross-diffusioncoefficients to zero results in a contradiction, and, the governing equationswithout cross-diffusion coefficients do not express the actual phase behaviorof the system.
机译:在经典的不可逆热力学框架下,采用Onsager变分原理,推导了三组分体系浓度和温度变化的控制方程,并提出了溶剂/溶剂/聚合物和溶剂/聚合物/聚合物体系。该推导是使用局部平衡假设,Onsager倒数关系和机械平衡的Prigogine定理从平衡热力学的吉布斯方程发展而来的。结果表明,三元系统中质量和热扩散现象的细节完全由一个3x3矩阵表示,其条目为质量扩散系数(4个条目),热扩散系数(2个条目)和三个描述系统热量演化的条目。扩散矩阵的项与Onsager矩阵的元素有关,这些元素受一些约束条件约束,以满足系统中熵产生的正定性。扩散矩阵的所有元素均以组分的交换化学势相对于浓度和温度的导数表示。由控制方程推导了三元聚合物溶液的旋节线曲线,并通过自由能密度的Hessian检验了其正确性。此外,证明了将交叉扩散系数设置为零会导致矛盾,并且没有交叉扩散系数的控制方程式不能表示系统的实际相位行为。

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