reactive distillation
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In Pro2, if the conversion rate of a reaction is defined, and reactive distillation is performed, can calculations still be carried out if this reaction is not present in Pro? 2 When performing reactive distillation, the product obtained is a component that is heavier than the reactants, and it is collected from the bottom of the tower. However, the gas-liquid load in the upper section of the tower is almost zero. What should be done in this case?
The liquid-holding capacity of each plate needs to be estimated by oneself and then entered for calculation
Why isn’t what I’ve made the product of the reaction? I hope some expert can give me some advice
The gas-liquid load in the upper section of the tower is almost 0; is it because the gas-liquid flow rate in the distillation section is very small? If so, it might be that the pressure set in your tower is too high, the temperature is too low, or the feed position is too low. I’m also a beginner, so please forgive me if what I say is incorrect