一种改进的溶液扩散中空纤维气体分离膜渗透模型:实现与分析

IF 1.6 4区 工程技术 Q3 ENGINEERING, CHEMICAL
Rama Alqassar Bani Almarjeh, Jason Yi Juang Yeo, Yomen Atassi, Seyed Saeid Hosseini, Jaka Sunarso
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引用次数: 0

摘要

致密聚合物中空纤维膜气体分离模块由于其与其他气体分离工艺相比具有更高的效率,在各种工业领域中变得越来越重要。膜气分离过程的建模和控制数学方程(如溶液-扩散模型)的分析是优化模块性能和提高工艺成本效益的关键。在此,我们介绍了一种改进的方法来求解聚合物中空纤维气体分离膜的数学模型,重点是更简单和更准确的求解策略。与以往的求解方法不同,模型特征函数(进料流量、渗透流量、进料成分、多孔支撑层内渗透成分、体渗透成分)更好地符合模块入口和封闭端的边界条件。改进后的算法求解精度更高,最大均方误差为7.3441 × 10−5,最小r2为0.8853,优于以往的复杂方法。修正后的算法还提高了速度,在0.015秒内完成计算,比任何报告的值都快。模型对几何和操作条件变化的响应通过广泛的灵敏度测试进行评估,该测试通过统计分析和数值解进行。与统计分析相比,数值解方法允许更广泛的相互作用可能性,并且可以检查更宽的响应面。此外,估计了渗透纯度、阶段切割纯度和保留纯度的响应方程,并针对不同的目标对工艺进行了优化。膜气分离性能对膜粒度和进料浓度高度敏感,这两个因素对分离驱动力有显著影响。因此,本研究提出了一种改进的求解策略,详细描述了各种参数对模型响应的影响,并对统计分析和过程优化可能性进行了全面比较。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
An Improved Permeation Model for Solution–Diffusion-Based Hollow Fiber Gas Separation Membrane: Implementation and Analysis

Dense polymeric hollow fiber membrane–based gas separation modules are becoming increasingly important in various industrial fields due to their higher efficiency compared to other gas separation processes. Modeling the membranes gas separation process and analyzing the governing mathematical equations such as the solution–diffusion model are crucial for optimizing module performance and making the process cost-effective. Herein, we introduce an improved methodology for solving the mathematical model of polymeric hollow fiber gas separation membranes focusing on a simpler and more accurate solution strategy. Unlike previous solving methods, the model characteristic functions (feed flow, permeate flow, feed composition, permeate composition within the porous support layer, and bulk permeate composition) better adhere to boundary conditions at the module inlet and closed-end. The improved solving algorithm provides a more accurate solution, with a maximum mean squared error of 7.3441 × 10−5 and minimum R 2 of 0.8853, outperforming previous complex methods. The corrected algorithm also features improved speed, completing calculations in under 0.015 s, faster than any reported values. The model's response to changes in geometric and operating conditions is evaluated through an extensive sensitivity test, which is conducted by statistical analysis and numerical solutions. Numerical solution approach allows for a wider range of possibilities of interactions compared to statistical analysis and enables inspection of a wider response surface. Additionally, the response equation is estimated for permeate purity, stagecut, and retentate purity, and the process is optimized for different goals. Performance of membrane gas separation is highly sensitive to the membrane sizing and feed concentration, as these factors significantly influence the separation driving force. Therefore, this study presents an improved solving strategy and a detailed description of the effect of various parameters on the model response, along with a comprehensive comparison to statistical analysis and process optimization possibilities.

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来源期刊
自引率
11.10%
发文量
111
期刊介绍: Asia-Pacific Journal of Chemical Engineering is aimed at capturing current developments and initiatives in chemical engineering related and specialised areas. Publishing six issues each year, the journal showcases innovative technological developments, providing an opportunity for technology transfer and collaboration. Asia-Pacific Journal of Chemical Engineering will focus particular attention on the key areas of: Process Application (separation, polymer, catalysis, nanotechnology, electrochemistry, nuclear technology); Energy and Environmental Technology (materials for energy storage and conversion, coal gasification, gas liquefaction, air pollution control, water treatment, waste utilization and management, nuclear waste remediation); and Biochemical Engineering (including targeted drug delivery applications).
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