旋转填料床二氧化碳物理化学吸收的计算建模与优化

Abdul Zahir, Perumal Kumar, Agus Saptoro, Milinkumar Shah, Angnes Ngieng Tze Tiong, Jundika Candra Kurnia, Samreen Hameed
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引用次数: 0

摘要

本研究开发了一种新型计算流体动力学(CFD)模型,该模型考虑了多相流中的物理和化学吸收,并通过采用可调模型参数 "增强因子 "来捕捉化学吸收相对于物理吸收的优势。该 CFD 模型根据旋转填料床的实验数据进行了验证,然后利用验证后的模型研究了旋转速度、单乙醇胺(MEA)浓度、入口速度和 MEA-填料接触角等操作参数对生化吸收的影响。然后通过方差分析评估了各操作参数的显著性,推断出增强因子对转速、MEA 浓度、进水速度和接触角很敏感。MEA 浓度和入口速度的 p 值小于 0.05,这意味着这两个变量是对二氧化碳化学吸收最重要的变量。此外,还采用了响应面方法(RSM)和人工神经网络(ANN)来建立增强因子的预测模型。在所采用的技术中,人工神经网络的 R2 值接近 0.99,能更好地预测增强因子。本研究的建模方法和结论有助于优化旋转填料床反应器(RPB)在工业规模上吸收二氧化碳的操作。
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Computational modelling and optimization of physicochemical absorption of CO2 in rotating packed bed
The current study developed a novel computational fluid dynamics (CFD) model that accounted for both physical and chemical absorption in the multiphase flow and captured the relative dominance of chemical absorption over physical by employing a tunable model parameter ‘enhancement factor’. The CFD model was validated against experimental data in a rotating packed bed, and then the validated model was used to investigate the effect of operational parameters such as rotational speed, monoethanolamine (MEA) concentration, inlet velocity, and MEA‐packing contact angle on the physiochemical absorption. The significance of each operational parameter was then evaluated by the ANOVA analysis, which inferred that the enhancement factor is sensitive to rotational speed, MEA concentration, inlet velocity, and contact angle. The p‐value of MEA concentration and inlet velocity was less than 0.05, which implies that these two variables are the most significant variables for the chemical absorption of CO2. The response surface methodology (RSM) and the artificial neural network (ANN) were also employed to develop the predictive model for the enhancement factor. Among the employed techniques, ANN resulted in R2 closer to 0.99 and could better predict the enhancement factor. The modelling approach and findings of the current study are useful in optimizing the operation of rotating packed‐bed reactor (RPB) for CO2 absorption on the industrial scale.
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