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机构地区:[1]National Laboratory of Secondary Resources Chemical Engineering, Zhejiang University, Hangzhou 310027, China [2]Department of Biological and Pharmaceutical Engineering, Ningbo Institute of Technology, Zhejiang University, Ningbo 315100, China
出 处:《Chinese Journal of Chemical Engineering》2006年第2期171-177,共7页中国化学工程学报(英文版)
基 金:Supported by the Doctoral Program Foundation of the Institution of Higher Education of China (No.20040335045).
摘 要:A rate model, which considers axial dispersion, external mass transfer, intraparticle diffusion and nonlinear isotherms, and ports periodic switching is adopted to simulate the simulated moving bed (SMB) process. The effects of flow rate in Sections 2 and 3 and switching time on the operating performance parameters: purity, recovery, productivity and dcsorbent consumption are studied. A simulation approach is applied to simulate the operation and performance of the SMB. The model predicts the performance of the transient and cyclic steady state behavior to a reasonably good extent, and provides guidance operation condition of the SMB process.A rate model, which considers axial dispersion, external mass transfer, intraparticle diffusion and nonlinear isotherms, and ports periodic switching is adopted to simulate the simulated moving bed (SMB) process. The effects of flow rate in Sections 2 and 3 and switching time on the operating performance parameters: purity, re- covery, productivity and desorbent consumption are studied. A simulation approach is applied to simulate the opera- tion and performance of the SMB. The model predicts the performance of the transient and cyclic steady state be- havior to a reasonably good extent, and provides guidance operation condition of the SMB process.
关 键 词:simulated moving bed MODELING SIMULATION soybean phosphatidylcholine
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