Tutorial on the use of Ponchon Savarit's method for distillation
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- Опубликовано: 6 фев 2025
- Calculation of number of trays for a distillation column is illustrated using the Ponchon-Savarit's method using the enthalpy diagram for saturated vapor enthalpy curve versus y and saturated liquid enthalpy of the mixture versus x. The diagram used is from Treybal's Mass Transfer Operations.
Nader Al-Bastaki Dept of Chemical Engineering University of Bahrain Mary 30th 2016
My prof did a poor job explaining this. You made it very easy to understand! Thank you, wish me luck on my separation processes midterm!
Thank you. You really explained this in a very concise and efficient manner. Really appreciate it!!
You are loved Prof.Nader Al-Bastaki. Thank you very much!!!
So glad I found this,thank you very much.
I'll like the video cause I know it's gonna help me in a near future. I'll be back in a few years when the time to use it finally comes. Till the I'll prepare myself the best I can and I give you my thanks in advancement.
Thank you for this tutorial, it makes this concept so much easier to understand.
Thank you very much sir. Cleared confusion at the feed line and the supporting section.
Thank you Nader Al-Bastaki, very cool
Very nicely explained. Helped me a lot. Thanks for that. Also, I would like to give a suggestion, please speak loud and clear from next time.
thank you, very well illustration
Beautiful explanation!
Thank you so much
It helped a lot sir.
I have a exam day after tomorrow can u draw a graph
which u have already made in this video.plz respond sir it's important
Really useful 👍
thank you for the demonstration you re a life saver :D
Thank you very much, Sir. It helped me a lot
Thanks a ton for this
Thank you, This helped a lot!
Thanks very much
ممتاز شرح واضح
amazing thsanks
Thank you 😭
Thanks a lot Professor
Thank you, very helpful
Thanks sir for ponchon method
I was here for more understanding
I think there is a mistake on how he find the stages because the 3 point that are in collinear are represent the operating line not the equilibrium
The three point ( differences point , Vn+1,Ln ) these are operating line
Thank you for the comment. The graphical representation for the stage is a linr between the ewuolibrium point
, which is the starting point on the vapour enthaloy dcurve and the final point on the liquid enthalpy curve. I have not drawn these lines. The line connecting to the reference point is the operating line as you have mentioned.
Thank you Sir🙌
Thank you sir.
Thanks
how is the condenser duty calculated ?
It's the amount of heat removed from your vapor at the topmost tray.
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Thank you very much :DDD
hahaha ez
Thanks