knapee
Petroleum
- Mar 9, 2011
- 100
Dear Professional engineer in the fourm
Sorry to bother you this trivial.
I tried to use simulation software such as pro ii, aspen plus
to find the latent heat of the multicomponent (the mixture also contain H2, N2).
I used three different flush drums to complete this job.
The first flash drum is set for duty=0, the second drum is set the
vapor fraction = 5%, and the third flush drum is set for the bubbling point.
After the simulation, I got the negative enthalpy on the last stream from the 3rd flush
drum liquid stream, and I wonder is the H2, N2 cause this negative result.
Then, I use the enthalpy in the stream of vapor from the 2rd drum substract the
enthalpy in the stream of liquid from the 3rd drum and substract the cp times the temperature difference
to get the latent heat.
But, our leader told me this negative enthalpy is impossible and I should
not input the H2, N2 stream infromation in the inlet stream in the pro ii or aspen.
Thank you very much for your comment and help.