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Experimental Study on Postcombustion Systems Including a Hollow Fiber Membrane and a Packed Column

[Image: see text] In this work, a comprehensive lab-scale carbon capture installation was established to study the separation performances of CO(2)/N(2) systems for the postcombustion technology. Four kinds of mono-/two-stage carbon capture methods containing membrane separation and chemical absorpt...

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Detalles Bibliográficos
Autores principales: Jiang, Yanchi, Zhang, Zhongxiao, Fan, Junjie, Yang, Liu, Liu, Jian
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2020
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7377326/
https://www.ncbi.nlm.nih.gov/pubmed/32715256
http://dx.doi.org/10.1021/acsomega.0c02251
Descripción
Sumario:[Image: see text] In this work, a comprehensive lab-scale carbon capture installation was established to study the separation performances of CO(2)/N(2) systems for the postcombustion technology. Four kinds of mono-/two-stage carbon capture methods containing membrane separation and chemical absorption processes were investigated. The result shows that the CO(2) capture performance of the one-stage membrane separation method (Memb) exhibits a profitable CO(2) removal efficiency but defective CO(2) concentration, while the one-stage chemical absorption method (Chem) indicates both CO(2) removal efficiency and CO(2) purity of more than 95.0% but suffers a regeneration heat of at least 2.7 MJ/t CO(2). The CO(2) purity of the two-stage membrane separation method (Memb–Memb) is 46.2% higher than the Memb method because of the additional membrane pretreatment. Two-stage methods have a superior gas recovery efficiency of over 99.0%, which is dramatically higher than the homogeneous Memb method. In addition, the investigation on the hybrid chemical absorption–membrane separation method (Memb–Chem) provides an alternative approach to reduce the mass transfer and solve the problems caused by an unequal mass flow distribution.