Ho Chii-Dong, Chang Hsuan, Tu Jr-Wei, Lim Jun-Wei, Chiou Chung-Pao, Chen Yu-Jie
Department of Chemical and Materials Engineering, Tamkang University, Tamsui, New Taipei 251, Taiwan.
Department of Fundamental and Applied Sciences, HICoE-Centre for Biofuel and Biochemical Research, Institute of Self-Sustainable Building, Universiti Teknologi PETRONAS, Seri Iskandar 32610, Perak Darul Ridzuan, Malaysia.
Membranes (Basel). 2022 Mar 29;12(4):370. doi: 10.3390/membranes12040370.
Theoretical predictions of carbon dioxide absorption flux were analyzed by developing one-dimensional mathematical modeling using the chemical absorption theory based on mass-transfer resistances in series. The CO absorption into monoethanolamine (MEA) solutions was treated as chemical absorption, accompanied by a large equilibrium constant. The experimental work of the CO absorption flux using MEA solution was conducted in double-unit flat-plate membrane contactors with embedded 3D turbulence promoters under various absorbent flow rates, CO feed flow rates, and inlet CO concentrations in the gas feed stream for both concurrent and countercurrent flow operations. A more compact double-unit module with embedded 3D turbulence promoters could increase the membrane stability to prevent flow-induced vibration and enhance the CO absorption rate by overwhelming the concentration polarization on the membrane surfaces. The measured absorption fluxes with a near pseudo-first-order reaction were in good agreement with the theoretical predictions for the CO absorption efficiency in aqueous MEA solutions, which was shown to be substantially larger than the physical absorption in water. By embedding 3D turbulence promoters in the MEA feed channel, the new design accomplishes a considerable CO absorption flux compared with an empty channel as well as the single unit module. This demonstrates the value and originality of the present study regarding the technical feasibility. The absorption flux enhancement for the double-unit module with embedded 3D turbulence promoters could provide a maximum relative increase of up to 40% due to the diminution in the concentration polarization effect. The correlated equation of the average Sherwood number was obtained numerically using the fourth Runge-Kutta method in a generalized and simplified expression to calculate the mass transfer coefficient of the CO absorption in the double-unit flat-plate membrane contactor with turbulence promoter channels.
通过基于串联传质阻力的化学吸收理论建立一维数学模型,分析了二氧化碳吸收通量的理论预测。将二氧化碳吸收到单乙醇胺(MEA)溶液中视为化学吸收,伴有较大的平衡常数。在双单元平板膜接触器中,在各种吸收剂流速、二氧化碳进料流速以及气体进料流中的入口二氧化碳浓度条件下,对采用MEA溶液的二氧化碳吸收通量进行了实验研究,实验采用了嵌入3D湍流促进器的双单元平板膜接触器,操作方式包括并流和逆流。一种带有嵌入3D湍流促进器的更紧凑的双单元模块可以提高膜的稳定性,防止流动引起的振动,并通过克服膜表面的浓度极化来提高二氧化碳吸收速率。在MEA水溶液中,测得的具有近似伪一级反应的吸收通量与二氧化碳吸收效率的理论预测结果吻合良好,结果表明该吸收效率远大于在水中的物理吸收。通过在MEA进料通道中嵌入3D湍流促进器,与空通道以及单单元模块相比,新设计实现了相当可观的二氧化碳吸收通量。这证明了本研究在技术可行性方面的价值和创新性。由于浓度极化效应的减小,带有嵌入3D湍流促进器的双单元模块的吸收通量增强可提供高达40%的最大相对增幅。使用四阶龙格-库塔方法以广义和简化表达式数值获得了平均舍伍德数的关联方程,用于计算带有湍流促进器通道的双单元平板膜接触器中二氧化碳吸收的传质系数。