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Dynamic Response/Characteristics of an Oxygen Swing Adsorption Process to Step Perturbations. Part 1 333 Figure 11. Change in feed moles per cycle due to a 5% increase in feed valve position — pilot plant, 313 mmol/cycle; model, 313 mmol/cycle. Figure 12. Change in feed moles per cycle due to a 10% decrease in product valve position — pilot plant, 31 mmol/cycle; model, 0 mmol/cycle. to Figure 4). Since the feed tank was at a much higher pressure than the adsorbent beds, choked flow conditions occurred in the process model, which resulted in a constant volumetric flow rate and subsequent molar rate as described by equation (6b). On the other hand, the pressure regula- tor fitted on the pilot plant decreased the feed tank pressure as experienced by the adsorbent beds and pressure-driven flow as described by equation (6a). The final point of note is that the response of the product stream flow to closure of the product valve and changes in load were very similar (not shown here). This is useful from a control per- spective since it means that a product-load disturbance can be simulated in the field by adjustmentPDF Image | Dynamic Response and Characteristics of an Oxygen Vacuum Swing Adsorption
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