CAPE-OPEN

Dear Jasper, I want to pose a question to your excellence, this is about my cases that I have solved in COCO in my M.Sc research, those cases involved alcoholic separations (separation of methanol from water, and separation of bio-ethanol from water that comes from fermentor in to the distillation c...

thanks in bundles sir!!!!
i really appreciate the commitment shown by your team for letting me know these points!!!

dear sir, i am facing a problem of handling a stream fed to chem sep UO column as a feed having co2 in it as a component of that stream. the problem is that COCO always asks me to check physical properties of co2 which seem OK. can you please help me out of this problem??? i am attaching a flowsheet...

dear sir (Mr.Jasper), i have been asked repeatedly by my supervisor to find out solubility of CO2 in water OR CO2 in ethanol-water mixture without considering electrolyte effect with henry's coefficient? but i do not know how can it be done ? can you please give me a clue of of any possible solution...

thanks a lot dear sir,
i really have gained so much of a help from your expertise and have a tremendous regard for helping and replying me with so much authenticity and practicability.
lots of regards!!!
Muhammad Shoaib
from
UET Peshawar
Pakistan.

i have been facing problem in finding the saturation solubility of Carbon dioxide in water, at different temperatures. can somebody help me in this regard??? secondly, when i am inserting a feed stream having carbon dioxide dissolved in water, my distillation column( chemsep UO) can not be solved. i...

dear sir, once again i have to seek help from your side that whether there is any procedure for process parameters sensitivity analysis in coco, as do we have in aspen plus??? if not, then whether is it appropriate to export our data from coco to excel and draw graphs showing sensitivity of variatio...

thanks a lot Mr. Jasper, its really been so cooperative and helpful discussion with you, throughout for me. my problem's been solved. bottom's temperature has also come within a real matchable range now. the only warning now that coco issues me is temperature range of liquid viscosity correlation is...

i have changed the column top pressure but it only gives an appropriate value of top product's temperature, bottom's remain the same. could you please check it what causes it to be same bottom product(waste's) temperature?

this is the case problem statement and procedure.