How to simulate a stripping tower? Thank you all
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As shown in the diagram, I want to simulate a diesel hydrodesulfurization stripping tower. The feed is as indicated; superheated steam is introduced at the bottom of the tower. There is no reboiler, and full reflux operation is used. The vapor phase emerges from the top of the tower, and water is separated in the reflux tank. The oil phase in the reflux tank is sent back to the tower as reflux. The tower actually has 24 trays – is it necessary to enter the tower efficiency value? How should this tower be simulated? Please help me out! How can the results of simulation be made identical to those in actual production?
Hello, may I ask what version of Aspen this is, and where can I find the Chinese translation?
v9, found it right in this basin
The question posed is too unclear; does this process really exist? Is it for simulated operating conditions, or for design and development?