Optimization of Multibed Pressure Swing Adsorption Processes
This work presents an optimization framework for complex pressure swing adsorption (PSA) processes including multibed configurations and multilayered adsorbents. The number of beds, PSA cycle configuration, and various operating and design parameters have been systematically optimized using recent a...
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Published in | Industrial & engineering chemistry research Vol. 48; no. 11; pp. 5388 - 5398 |
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Main Authors | , , |
Format | Journal Article |
Language | English |
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Washington, DC
American Chemical Society
03.06.2009
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Abstract | This work presents an optimization framework for complex pressure swing adsorption (PSA) processes including multibed configurations and multilayered adsorbents. The number of beds, PSA cycle configuration, and various operating and design parameters have been systematically optimized using recent advances on process optimization. The Unibed principle has been adopted relying on the simulation over times of only one bed while storage buffers have been used to model bed interactions. A novel state transition network (STN) representation is employed for the efficient simulation and optimization of the processes. Two large-scale multicomponent separation processes have been used to illustrate the applicability and potential of the proposed approach in terms of improvement of product purity and recovery. Results indicate that significant improvements can be achieved over base case designs. |
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AbstractList | This work presents an optimization framework for complex pressure swing adsorption (PSA) processes including multibed configurations and multilayered adsorbents. The number of beds, PSA cycle configuration, and various operating and design parameters have been systematically optimized using recent advances on process optimization. The Unibed principle has been adopted relying on the simulation over times of only one bed while storage buffers have been used to model bed interactions. A novel state transition network (STN) representation is employed for the efficient simulation and optimization of the processes. Two large-scale multicomponent separation processes have been used to illustrate the applicability and potential of the proposed approach in terms of improvement of product purity and recovery. Results indicate that significant improvements can be achieved over base case designs. |
Author | Kikkinides, Eustathios S Nikolić, Dragan Georgiadis, Michael C |
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Cites_doi | 10.1002/aic.690450310 10.1016/S1383-5866(00)00191-X 10.1016/0009-2509(90)80176-F 10.1002/aic.10223 10.1002/aic.690401207 10.1016/0009-2509(93)80114-6 10.1021/ie00068a014 10.1081/SS-120014437 10.1081/SS-100100183 10.1002/aic.10400 10.1002/aic.690490508 10.1023/A:1008925703871 10.1021/ie0615180 10.1023/A:1008823102106 10.1016/0009-2509(89)85090-0 10.1002/aic.690440610 10.1002/aic.690460413 10.1016/S0009-2509(03)00189-1 10.1002/aic.690340902 10.1021/ie049032b 10.1016/S0009-2509(98)00196-1 10.1016/0009-2509(94)85035-6 10.1080/00986448608911718 10.1016/0009-2509(91)85001-E 10.1021/ie00033a015 10.1021/ie0712582 10.1016/S0255-2701(98)00044-0 10.1021/ie00023a042 |
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Title | Optimization of Multibed Pressure Swing Adsorption Processes |
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