溶解度计算方法、装置及存储介质

By adding perturbations to the mole fraction of multi-component mixtures and constructing the Jacobian partial derivative matrix, the PCSAFT model was used to solve the problems of high complexity and slow convergence speed in multi-component vapor-liquid phase equilibrium calculations. Fast and accurate convergence of phase equilibrium points was achieved, and the calculation results are in good agreement with experimental data.

CN119007877BActive Publication Date: 2026-07-17EAST CHINA UNIV OF SCI & TECH +1

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
EAST CHINA UNIV OF SCI & TECH
Filing Date
2024-08-05
Publication Date
2026-07-17

AI Technical Summary

Technical Problem

Existing technologies suffer from high computational complexity, slow convergence speed, and difficulty in accurately converging to the phase equilibrium point when dealing with vapor-liquid phase equilibrium of multi-component mixtures, especially in complex systems such as high-concentration and polar solutions.

Method used

By adding perturbations to the mole fractions of multiple components, a multidimensional Jacobian partial derivative matrix is ​​constructed, and each component is updated synchronously. Using the PCSAFT residual Helmholtz energy model and thermodynamic equilibrium conditions, the system converges quickly and accurately to the phase equilibrium point.

Benefits of technology

It achieves rapid and accurate convergence of the vapor-liquid phase equilibrium problem of multi-component mixtures, with the average error between the calculation results and experimental data not exceeding 3.98%, thus improving computational efficiency and accuracy.

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Abstract

本发明提供了一种溶解度计算方法、一种溶解度计算装置及一种计算机可读存储介质。所述溶解度计算方法包括以下步骤:设定烯烃聚合体系中多个组分在气、液两相中的初始摩尔分数、初始温度、初始压力、各所述组分的物质参数,以及各所述组分之间的二元交互参数。各所述组分在气、液两相中的初始摩尔分数之和分别为1;计算各所述组分在气、液两相的逸度,并据此设置逸度相关的气液相平衡条件;以及响应于各所述组分的摩尔分数满足所述气液相平衡条件,根据至少一个液相组分的摩尔分数,求解其在所述烯烃聚合体系中的溶解度。本发明可以用于解决多组分混合物的汽液相平衡问题,从而快速且准确地收敛到相平衡点。
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