Sustainability Improvement of Membrane Separation Process for Post-Combustion CO2 Capturing Using Multi-Objective Optimization

J. Asadi, P. Kazempoor
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Abstract

The membrane process is a promising technology for CO2 removal and mitigation. Since the energy consumption and economy of membrane-based carbon capture systems (CCSs) are critical for their large-scale deployments, optimal design and operation of such systems are the primary aims of this study. To achieve these research goals, a numerical model based on the solution-diffusion mechanism for the multicomponent gas separation process with a hollow-fiber membrane module is developed using Aspen Custom Modeler. The model is employed to investigate the effects of important operating and design parameters. Multi-objective process optimization is then performed by linking Aspen Plus and MATLAB and using an evolutionary technique to determine the optimal operating and design conditions. Our results show that by increasing the CO2 concentration in the feed gas, the CO2 capture cost significantly decreases and CO2 removal improves, although the process energy requirement slightly increases. The best achievable tradeoffs between objective functions are generated and analyzed, which substantiate the significant potential for improving the sustainability of the process. The results show that at optimum design and operating conditions, CO2 capture cost and energy consumption of the process could be as low as 13.1 $/tCO2 and 61 MW, respectively. The results of this study provide valuable insights into membrane separation and can be used by decision-makers to achieve the optimal performance of the process for commercial development and deployment of the technology.
利用多目标优化提高燃烧后CO2捕集膜分离工艺的可持续性
膜法是一种很有前途的CO2去除和减缓技术。由于膜基碳捕获系统(ccs)的能耗和经济性对其大规模部署至关重要,因此该系统的优化设计和运行是本研究的主要目的。为了实现这些研究目标,利用Aspen Custom Modeler开发了一个基于溶液扩散机制的中空纤维膜组件多组分气体分离过程的数值模型。利用该模型研究了重要的运行参数和设计参数的影响。然后,将Aspen Plus与MATLAB相结合,采用进化技术进行多目标过程优化,以确定最佳运行和设计条件。我们的研究结果表明,通过增加原料气中的CO2浓度,CO2捕集成本显著降低,CO2去除率提高,尽管过程能量需求略有增加。生成并分析了目标函数之间可实现的最佳折衷,这证实了改进过程可持续性的重大潜力。结果表明,在最佳设计和运行条件下,该工艺的CO2捕集成本和能耗分别可低至13.1美元/tCO2和61 MW。这项研究的结果为膜分离提供了有价值的见解,可以为决策者提供决策依据,以实现该工艺的最佳性能,从而实现该技术的商业开发和部署。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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