Are there any seniors or peers who have experience with Aspen adsorption, so that we can help each other improve?

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Are there any seniors or peers who have experience with Aspen adsorption, so that we can help each other improve? I’m interested in exchanging ideas regarding learning*. My QQ number is 2549834061. I warmly welcome anyone willing to engage in such exchanges; I’m looking for partners who can inspire each other and help us improve. Gas_valve model – control valves: a. Used as controls to open or close valves; b. Function as reversible flow regulators, allowing control over the flow rate through the valves as well as the direction of flow: feed valves VF, VF1, VF2; drain valves VW1 and VW2; purge valve VPurge; product valves VP, VP1, VP2. Gas_tank_void model: Acting as a mixer or separator, as well as a pressure setter, it calculates the flow rate using valve equations based on the pressure drop across the valves and the pressure drop across the adsorption bed. 1. TF serves as the pressure setter, fixing the pressures between valves VF and VF1, as well as between valves VF and VF2. 2. Add the gas_tank_void block TW as a pressure setter to fix the pressure between VW1 and VW, as well as the pressure between VW2 and VW. 3. Add the gas_tank_void block TP as a pressure setter to fix the pressure between VP1 and VP, and the pressure between VP2 and VP. 4. Add T1a and T1b gas cylinder blocks as pressure setters to fix the inlet and outlet pressures of adsorption bed B1. By doing this, we also fixed the pressure between valves VF1 and VW1, as well as the pressure between valves VPurge and VP1. 5. Add T2a and T2b gas cylinder blocks as pressure setters to fix the inlet and outlet pressures of adsorption bed B2. By doing this, we also fixed the pressure between valves VF2 and VW2, as well as the pressure between valves VPurge and VP2.