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334 C.C.K. Beh and P.A. Webley/Adsorption Science & Technology Vol. 21 No. 4 2003 Figure 13. Change in evacuation moles per cycle due to a 5% increase in feed valve position — pilot plant, 188 mmol/cycle; model, 237 mmol/cycle. Figure 14. Change in evacuation moles per cycle due to a 10% decrease in product valve position — pilot plant, 31 mmol/cycle; model, 56 mmol/cycle. of the product valve alone. This is much easier to effect in practice than the application of an actual load disturbance. This result was expected. Effect of process disturbances on oxygen purity Product concentration (%O2) is arguably the most important variable from the perspective of a customer and consequently demands tight control tolerances (typically ± 1% of set point).PDF Image | Dynamic Response and Characteristics of an Oxygen Vacuum Swing Adsorption
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