Dear Collins Mordi, good evening! Thank you for your time sharing this important example related to absorbers and Hysys. I would like to know if you are open to talk about this same example but more focused on real sizing the absorber (dimensions). The efficiency - 90% - adopted by you is really achievable on real world? Would you like to talk more about it? Would be great if the answer is yes ! :D
Hi. Thank you for posting this. I am trying a tutorial with an absorber, but a different set of components (CH4 and CO2), but keep getting a weird error about one of the stages. I was wondering if there is any way you could help.
Dear Collins Mordi, good evening! Thank you for your time sharing this important example related to absorbers and Hysys. I would like to know if you are open to talk about this same example but more focused on real sizing the absorber (dimensions). The efficiency - 90% - adopted by you is really achievable on real world? Would you like to talk more about it? Would be great if the answer is yes ! :D
The H2SO4 feed stream introduced the composition in mole fraction and should be in mass fraction....
gracias sr usted es un genio
Hi. Thank you for posting this. I am trying a tutorial with an absorber, but a different set of components (CH4 and CO2), but keep getting a weird error about one of the stages. I was wondering if there is any way you could help.
Hello, my temperature solution is equal 45°C I don't Understand why?
And you temperature is equal 30°C
Thank you
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Sir temperature is optional only know hysys by itself will calculate for us then, why you specify it here.
BIbliografia xd
Hello Collins, does the simulation account for the heat of reaction between Sulfuric acid and ammonia to form ammonium sulfate?