Find the formula for the p-xylene disproportionation stripping tower.
Thread Content
Design a p-xylene disproportionation stripping tower. Benzene, toluene, mixed xylene, etc., which come out of the high-pressure tank, enter the stripping tower for separation. As shown in Figure 1, product C6 is generated at the bottom of the tower, while non-condensable gases are produced at the top. Figure 2 shows the feeding process; some of it can be removed. I would like to ask whether this calculation can be done using the formulas for distillation columns? (Haven’t studied stripping towers)
I don’t know either; it disappeared as soon as I uploaded it. I’ll upload it again
The HaiChuan app for mobile phones is full of bugs. . . It was uploaded and then disappeared