×
INTELLIGENT WORK FORUMS
FOR ENGINEERING PROFESSIONALS

Log In

Come Join Us!

Are you an
Engineering professional?
Join Eng-Tips Forums!
  • Talk With Other Members
  • Be Notified Of Responses
    To Your Posts
  • Keyword Search
  • One-Click Access To Your
    Favorite Forums
  • Automated Signatures
    On Your Posts
  • Best Of All, It's Free!
  • Students Click Here

*Eng-Tips's functionality depends on members receiving e-mail. By joining you are opting in to receive e-mail.

Posting Guidelines

Promoting, selling, recruiting, coursework and thesis posting is forbidden.

Students Click Here

Jobs

re: Compressible Flow Modelling

re: Compressible Flow Modelling

re: Compressible Flow Modelling

(OP)
Hi,

I am working on a study to determine the peak pressure and temperature as a result of a steam discharge (T= 300C, 500 kg/hr)into a CO2 low pressure circuit with the compressors operating at P=11 psig and Q=5 L/s.   

I am thinking about using saturated steam (P =1 atm T=100C) for the modelling as the software that I am using doesn't have CO2.  Secondly, the discharge steam will purge the CO2 very quickly.  

For the steady-state, I was thinking that using the sat. steam and to adjust the pressure drop of the circuit to match the operating flow for CO2.

I was wondering if anyone can give some pointers if these assumptions are feasible?   

Red Flag This Post

Please let us know here why this post is inappropriate. Reasons such as off-topic, duplicates, flames, illegal, vulgar, or students posting their homework.

Red Flag Submitted

Thank you for helping keep Eng-Tips Forums free from inappropriate posts.
The Eng-Tips staff will check this out and take appropriate action.

Reply To This Thread

Posting in the Eng-Tips forums is a member-only feature.

Click Here to join Eng-Tips and talk with other members!


Resources