Thanks for your reply. Yes, it would be still dependent on the inlet pressure but independent of inlet temperature. In case of an actual flow though, with the actual flow being dependent on both pressure and temperature, the discharge pressure would become dependent on both inlet pressure and...
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...
Thanks all for answering. My steam is saturated and it becomes two phase along the pipe (coming from OTSGs). What I have seen so far, comparing to plant data, the pressure drop with Beggs and Brill (1979) correlation in HYSYS V7.3 is almost double that of other HYSYS Pipe Segment correlations...
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).
