期刊
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
卷 43, 期 4, 页码 1150-1162出版社
AMER CHEMICAL SOC
DOI: 10.1021/ie030630k
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Rotating packed beds have received considerable attention as a means of process intensification for gas-liquid mass transfer over the past 2 decades. In this work, we take a critical view of the developments in understanding the transport processes in rotating packed beds. The intensification achieved so far falls short of the goal of 2-3 orders of magnitude volume reduction compared to that obtained conventional columns. The directions toward achieving this goal are outlined.
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