Reactive Distillation using Aspen HYSYS

  Рет қаралды 18,743

GómezM_O

GómezM_O

Күн бұрын

Пікірлер: 11
@muhammadshehreyarkhan1851
@muhammadshehreyarkhan1851 9 жыл бұрын
Nice one brother ! I owe you
@sali3323
@sali3323 9 жыл бұрын
Thanks bro...the video was very helpful
@osgomefw
@osgomefw 9 жыл бұрын
You're welcome. Successes.
@ash1704ful
@ash1704ful 10 жыл бұрын
why is the first stage 37 and the last stage 4 when inputting the reaction?
@jaylokhaha8679
@jaylokhaha8679 9 жыл бұрын
Hello, may i know how did you determine the inlet feed stage for both reactants?
@jayasenan
@jayasenan 8 жыл бұрын
+Jay LokHAHA use a split column first. then replace the split column with the distillation column above
@ruthemberru-ekperiware8306
@ruthemberru-ekperiware8306 10 жыл бұрын
hello,nice work you've done here. Am using Aspen Hysys V8.0, and it does not specify reaction components. Please help. Thanks
@osgomefw
@osgomefw 10 жыл бұрын
Hello Ruth, unfortunately we worked in this Project 4 years ago and really I don't remember well how to proceed with new Aspen versions. Good luck!
@ruthemberru-ekperiware8306
@ruthemberru-ekperiware8306 10 жыл бұрын
Osnaider Gómez Mejía pls send your email address to ruthina04@yahoo.com thanks
@jikichong342
@jikichong342 7 жыл бұрын
Hi, could you please do one on Aspen plus?
@nelsoneuadaba3088
@nelsoneuadaba3088 8 жыл бұрын
HELLO BRO... Help me do this: The design task for the separation of ethyl acetate - butyl acetate mixture. For the separation of binary mixtures, continuous distillation process. Design uses 60 ℃-feeding, the liquid raw material fed into the rectification column. Rise with full overhead vapor condenser condensate, the condensate is returned to the part of the bubble point under the tower, the rest of the product after the condenser to the cooling tank. Bottoms indirect steam heating, bottoms after cooling to the storage tank. Recovery of overhead and bottoms D = 6.660kmol / h, W = 9.287kmol / h
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