Jump to content



Featured Articles

Check out the latest featured articles.

File Library

Check out the latest downloads available in the File Library.

New Article

Product Viscosity vs. Shear

Featured File

Vertical Tank Selection

New Blog Entry

Low Flow in Pipes- posted in Ankur's blog

Lpg (Mixtures) Calculation Of Pressure


This topic has been archived. This means that you cannot reply to this topic.
2 replies to this topic
Share this topic:
| More

#1 NestorMadeo

NestorMadeo

    Brand New Member

  • Members
  • 1 posts

Posted 23 January 2012 - 02:29 PM

Hi, I need the formula to calculate the pressure of LPG in their various mixtures, with the temperature and density.
For example: 100% propane at -42 ° C to pressure you.
Thank you ... regards
Nestor

Attached Files

  • Attached File  LPG.jpg   928.34KB   36 downloads


#2 ankur2061

ankur2061

    Gold Member

  • Forum Moderator
  • 2,484 posts

Posted 23 January 2012 - 11:28 PM

Your query is not very clear. I am assuming that you are looking for the vapor pressure of LPG at various temperatures. Basically this requires the Antoine equation for the individual components which has the following general form:

log10Pi = A - B/(t+C)

where:

Pi = vapor pressure of the ith component, mmHgA

A = constant 1 for ith component
B = constant 2 for ith component
C = constant 3 for ith component
t = reference temperature, °C

Vapor pressure of mixture

Pmix = Σxi*Pi

where:

Pmix = VP of mixture, mmHgA
xi = mole fraction of the component
Pi = VP of the ith component, mmHgA

A vapor pressure calculator for pure compounds is available on "Cheresources" at:

http://www.cheresour...h&fromMainBar=1

Hope this helps.

Regards,
Ankur.

#3 MrShorty

MrShorty

    Gold Member

  • ChE Plus Subscriber
  • 517 posts

Posted 24 January 2012 - 10:50 AM

As Ankur suggests, using Raoult's law is certainly the easiest method for calculating the vapor pressure of mixtures. And, if I assume as suggested by your chart that LPG to you means "mixtures of C2-C4 aliphatic hydrocarbons," then Raoult's law is probably good enough for most applications. I would check it against your chart to see how much error this "ideal" computation has.

If you want to get really excited, you can incorporate activity and/or fugacity coefficients into your calculation. Computational difficulty goes up quite quickly, though. Only you can judge if, in your case, the improved accuracy is worth the extra effort.




Similar Topics