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330 C.C.K. Beh and P.A. Webley/Adsorption Science & Technology Vol. 21 No. 4 2003 Figure 6. Pressure history for bed 1. Comparison of plant and model over a single cycle. Figure 7. Product tank pressure history whilst undergoing feed from bed 2 (step 5) for a step change in the feed valve position — comparison of plant and model. Change in pressure: pilot plant, ~3.9 kPa; model, 4.54 kPa. profile was manifested in the product tank pressure and resulted in similar mismatches between the plant and model as shown in Figure 8. Although the difference between the model and plant pressure history (Figure 6) appear to be large, it is important to note that the pressure scale was deliberately exaggerated to help highlight the differences. In addition, it should be remembered that the true ‘long time scale’ cyclic steady state was not attained within the 12 cycles shown in Figures 5 and 7. Despite these points, the pres- sures reached constant values and, interestingly, retained these values even at true cyclic steadyPDF Image | Dynamic Response and Characteristics of an Oxygen Vacuum Swing Adsorption
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