Pressure-Swing Distillation to separate Ethanol-Water Mixture | Aspen HYSYS | Lecture # 27
ฝัง
- เผยแพร่เมื่อ 21 ส.ค. 2020
- Learn how to use pressure-swing distillation technique to separation ethanol-water mixture. This technique makes use of two columns, operating at different pressures to cause separation of the mixture, which are not easy to separate using conventional distillation scheme. Please do watch, like, and share the video, and subscribe the channel. Please provide your feedback for the improvement.
Problem Statement:
A feed mixture consisting of 20 mol% ethanol, and 80 mol% water is fed to the low-pressure column at 1.2 bar, 65 °C, and a mass flowrate of 24,000 kg/h.
LP Column: 30 stages, 25th feed stage, condenser and reboiler pressure as 0.1 bar. 99% recovery of ethanol, and 90 mol% ethanol in the top of the LP column.
Pump: the top product of LP column is pumped to high-pressure column at 20 bar.
HP Column: 75 stages, 40th feed stage, condenser and reboiler pressure as 20 bar. 99 mol% ethanol in the bottom, bottom product flowrate as 200 kgmole/h.
Recycle stream with the following specifications:
(vapor fraction = 0; pressure = 1.2 bar; flowrate = 400 kgmole/h, 90 mol% ethanol, and 10 mol% water).
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#Ethanolwatermixture
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Mashallah the lectures are very easy to grasp such easily explained.....
Glad to hear that
Completed lec 27
Thank so much, salve me!!!
شكرا 🌹😊
VERY GOOD WORK🤩
MasahAllah very good work, easy to understand suggestion: please also do in aspen plus
dear, I have need of simulation video which contain purification of ethanol from fusel oil along with short cut distillation colomn
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Hello, thank you for your good videos. Do you have a channel in Telegram or software that provides us with hysys and Word question files?
Sir, my HP Seeperator is converging without recycle any comments?
Yes. It will. Recycling is done to avoid wastage of solvent.
Can you make a video of PSA unit
Adsorption module is not available in Aspen.
What if we don’t have recycle stream? How can we do this?
After connecting recycle stream, my simulation is falling apart...
Reached iteration limit without converging
If somebodys here with the same problem, try checking all of streams, especially after connecting valve. My problem was, restream was too hot and vapour occured so i implemented an additional cooler