I am simulating a centri. compressor via Aspen One. I know how to do this in general, but want to clear up a confusion.
I have two types of performance curves from manufacturer: Pressure Ratio vs Std Flow and Pressure Ratio vs Actual Flow.
Aspen One gives two options to you for specifying...
We have a case in which when we cut off the inlet feed to an exothermic reactor (feed is gas) the temperature in the reactor still rises for a while. Given that we expect it almost immediately stops rising our first guess is that there is a delay with temperature sensors within the reactor. Any...
Just wondering what is the best correlation to be used in a pipe segment of HYSYS for steam? (the closest one to reality for finding the pressure drop of a pipe).