Thankfully now i can design a distillation column from scratch to the internal designing of distillation column, this i did by following your every single video in series ( lecture wise) . Very dedicated efforts from your side Sir. Thanks a lot
Well explained I just have a question regarding the internal designing, Should we stock with the giving diameters or should we round them to the next standard diameter and make both sections with the same diameter?
Please, tell me how to calculate the pressure drop across the column, I press the "export pressure drop" button, but HYSYS says that this value is set, but if I remove it, the convergence of the column breaks down (red colour) and internal devices become impossible to calculate
Hello sir, My name is Agus. I'm sorry if my english typing is not well I want to ask about K-values. Until right now, I'm still confused about how to estimating K-values components in vapor-liquid separation processes in aspen hysys I hope you can give me a reason or explanation about it. I really apreciate, if u can respon this question. Thanks sir Sincerely
How to reduce the amount of vapor at the top of the rectification column? The type of trays, their efficiency? I have a lot of top reflux in model the unisim program. I am asking for an answer and best
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Thankfully now i can design a distillation column from scratch to the internal designing of distillation column, this i did by following your every single video in series ( lecture wise) .
Very dedicated efforts from your side Sir.
Thanks a lot
Good explanation! atleast came to know how to use short cut distillation...Thank you!
Welcome dear Nasir.
Great work. thanks
Thank you Saeid
Thanks prof! Very helpful
You are welcome!
Good job, brother
Thank you for the appreciation.
Well explained
I just have a question regarding the internal designing,
Should we stock with the giving diameters or should we round them to the next standard diameter and make both sections with the same diameter?
Completed lec-21
Please, tell me how to calculate the pressure drop across the column, I press the "export pressure drop" button, but HYSYS says that this value is set, but if I remove it, the convergence of the column breaks down (red colour) and internal devices become impossible to calculate
Thank you bro very clear
have you explained on batch distillation aspen?
Hello sir, My name is Agus. I'm sorry if my english typing is not well
I want to ask about K-values. Until right now, I'm still confused about how to estimating K-values components in vapor-liquid separation processes in aspen hysys
I hope you can give me a reason or explanation about it. I really apreciate, if u can respon this question.
Thanks sir
Sincerely
How to reduce the amount of vapor at the top of the rectification column? The type of trays, their efficiency? I have a lot of top reflux in model the unisim program. I am asking for an answer and best
You can reduce the top flow rate by specifying value of flow rate in the specifications tab. And same goes for reflux ratio
Thank you very much for help. I will check
Thanks for your dedicated video, Sir. I have 1 question: What is the difference between "Column Environment" and "Parent Environment"?
Parent environment shows the column characteristics in detail, like reflux pump, etc.
@@aspenchemchannel Thank you Sir!
Good, But how you decided condenser pressure 5 bar and reboiler pressure 4.8?
Assuming a pressure drop of 0.2 bar in condenser and no pressure drop in reviler.
can we do autosection on the basis on flow rate?
Yes. Just click on scroll button beside the auto section. It will give you two options. Flow rate and feed draw locations.
can you give me your mail id?? I have to ask something related to my project on aspen plus