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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Mathematical calculation of binodal curves of a polymer/solvent/ nonsolvent system in the phase inversion process
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Mathematical calculation of binodal curves of a polymer/solvent/ nonsolvent system in the phase inversion process

机译:相转化过程中聚合物/溶剂/非溶剂体系二项式曲线的数学计算

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摘要

Four methods of calculating Flory-Huggins interaction parameters from solubility parameters were examined by comparing calculated binodal curves with experimental data.This is a promising method to calculate interaction parameters from solubility parameters because of the wide use of solubility parameters.The fitting results were satisfactory after the optimization of the correction constant according to the membrane casting systems mentioned.The optimized correction constants were 0.09 and 1.01 for the polymer/solvent and polymeronsolvent,respectively.The constants were obtained from PES/solvent and PSF/solvent systems and checked with PSF/DMAconsolvent systems.Calculation was carried out,based on Flory-Huggins solution theory,to analyze the behavior of the polymer/solventonsolvent system phase diagram with the influence of parameter sets in a wide range.It was found that with the increment of solvent/polymer interaction parameters or nonsolvent/porymer interaction parameters the miscibility gaps decreased.However,the miscibility gaps increased with the increment of nonsolvent/solvent interaction parameters.
机译:通过比较计算出的二元曲线与实验数据,检验了由溶解度参数计算Flory-Huggins相互作用参数的四种方法,由于溶解度参数的广泛使用,这是一种从溶解度参数计算相互作用参数的有前途的方法,拟合结果令人满意聚合物/溶剂和聚合物/非溶剂的最佳校正常数分别为0.09和1.01。从PES /溶剂和PSF /溶剂系统获得的常数经过PSF / DMAc /非溶剂体系。基于Flory-Huggins溶液理论进行了计算,在较大的参数集影响下分析了聚合物/溶剂/非溶剂体系相图的行为。溶剂/聚合物相互作用参数或非溶剂/聚合物相互作用参数的增量混溶间隙减小。但是,混溶间隙随着非溶剂/溶剂相互作用参数的增加而增加。

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