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
Nice one brother ! I owe you
Thanks bro...the video was very helpful
You're welcome. Successes.
why is the first stage 37 and the last stage 4 when inputting the reaction?
hello,nice work you've done here. Am using Aspen Hysys V8.0, and it does not specify reaction components. Please help. Thanks
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!
Osnaider Gómez Mejía pls send your email address to ruthina04@yahoo.com
thanks
Hello, may i know how did you determine the inlet feed stage for both reactants?
+Jay LokHAHA use a split column first. then replace the split column with the distillation column above
Hi, could you please do one on Aspen plus?
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