Process modeling and sensitivity analysis of intensified post-combustion CO2 capture process by polyamine solution in a rotating packed bed

IF 7.5 1区 工程技术 Q2 ENERGY & FUELS Fuel Pub Date : 2025-10-01 Epub Date: 2025-04-21 DOI:10.1016/j.fuel.2025.135294
Mohammad Shamsi , Jafar Towfighi Darian , Morteza Afkhamipour
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Abstract

This study explores a modeling-optimization approach for CO2 capture using polyamine, diethylenetriamine (DETA), in a rotating packed bed. The developed model is based on a rate-based approach and the Deshmukh-Mather model as the thermodynamic framework, which is incorporated into the rate-based model. Various mass transfer correlations are employed to conduct a sensitivity analysis based on an orthogonal array design. The model outcomes were validated by comparing them with experimental data from the literature. All profiles along the radial direction were predicted, including gas and liquid concentrations (both molecular and ionic species), gas and liquid flow rates, temperatures, and pressure. The impact of RPM on CO2 capture level was examined under different amine concentrations, amine temperatures, amine and gas flow rates, and pressure. Additionally, the effect of RPM on liquid hold-up was analyzed. The findings indicate that the rate-based model accurately predicts the experimental data, with an AARD of 3.015%. Furthermore, the most suitable correlations for mass transfer coefficients in the gas and liquid phases, as well as the effective surface area, were identified using sensitivity analysis to evaluate CO2 absorption by the DETA solution in an RPB. Finally, the OAD method was employed for statistical optimization and ranking of key operating parameters that simultaneously influence CO2 capture performance. The RPB absorber was optimized based on three factors: rotational speed, lean amine temperature, and flow rate. The rate-based model was employed to predict the response values (CO2 capture level) in the OAD method. The OAD outcomes reveal that rotational speed and solvent temperature have the greatest impact on CO2 capture level, respectively. Furthermore, a comparative analysis demonstrates that the RPB exhibits superior mass transfer performance under identical operating conditions compared to a conventional packed column with Dixon ring packing.
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旋转填料床中多胺溶液强化燃烧后二氧化碳捕获工艺的工艺建模和敏感性分析
本研究探索了在旋转填充床中使用多胺,二乙烯三胺(DETA)捕获二氧化碳的建模优化方法。所开发的模型是基于基于速率的方法,并将Deshmukh-Mather模型作为热力学框架纳入到基于速率的模型中。在正交阵列设计的基础上,采用各种传质相关性进行灵敏度分析。通过与文献实验数据的比较,验证了模型结果。预测了沿径向的所有剖面,包括气体和液体浓度(包括分子和离子)、气体和液体流速、温度和压力。在不同的胺浓度、胺温度、胺和气体流速以及压力下,考察了转速对CO2捕集水平的影响。此外,还分析了转速对液持率的影响。结果表明,基于速率的模型能够准确预测实验数据,AARD为3.015%。此外,通过灵敏度分析,确定了气相和液相传质系数以及有效表面积的最合适相关性,以评估RPB中DETA溶液对CO2的吸收。最后,采用OAD方法对同时影响CO2捕集性能的关键运行参数进行统计优化和排序。根据转速、精胺温度和流量三个因素对RPB吸收塔进行了优化。采用基于速率的模型预测OAD方法的响应值(CO2捕获水平)。OAD结果表明,转速和溶剂温度分别对CO2捕集水平影响最大。此外,对比分析表明,在相同的操作条件下,与传统的Dixon环填料柱相比,RPB具有更好的传质性能。
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来源期刊
Fuel
Fuel 工程技术-工程:化工
CiteScore
12.80
自引率
20.30%
发文量
3506
审稿时长
64 days
期刊介绍: The exploration of energy sources remains a critical matter of study. For the past nine decades, fuel has consistently held the forefront in primary research efforts within the field of energy science. This area of investigation encompasses a wide range of subjects, with a particular emphasis on emerging concerns like environmental factors and pollution.
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