Estimating density, viscosity and thermal conductivity

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Estimating the density, viscosity, and thermal conductivity of a gaseous mixture at 20 bar involves using the ideal gas law and specific equations for mixtures. The user has all necessary pure component data from NIST but finds that a simple weighted average of properties based on mole fractions may not yield accurate results. They have consulted Perry's engineering handbook and design textbooks without finding a reliable method. Attempts to incorporate the compressibility factor into calculations resulted in unrealistically low density values. For accurate mixing rules, referencing "Transport Phenomena" by Bird et al is recommended.
Mark Rice
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Homework Statement


Hi there, I am designing a heat exchanger and I am really struggling to find out how to fairly accurately estimate the density, viscosity and thermal conductivity of a gaseous mixture at ~~20bar. There is 8 components in the mixture: methane, ethane, ethene, ethlyene oxide, CO2, water, argon and O2.

Homework Equations


PV=znRT (for denisty),
kmix = ka Ma + kbMb + knMn (for themal conductivity of mix

I have all the pure component values of density, viscosity and thermal conductivity from NIST at the correct P and T.

The Attempt at a Solution


My initial thought was to just simply do a weighted average of the sum of (properties*molefraction) however I feel this may not be that accurate. I have looked through perry's engineering handbook and some design textbooks and can't find a reliable method to work out these properties. I then tried to use the ideal gas law with the compressibility factor however the values this gave me Z was almost = 1 and my density values were way too low (I know what the values should be roughly as I have modeled it on design software).

Thanks,
 
Last edited:
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See Transport Phenomena by Bird et al for mixing rules.
 

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