Explicit natural gas viscosity correlation:
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| \mu_g = K \cdot \exp \left( X \, \rho_g^Y \right) |
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100 < T < 340 °F
100 < p < 8,000 psi
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| K = T^{1.5} \cdot \frac{9.379 + 0.01607 \, MW_g}{209.2 + 19.26 \, MW_g +T} |
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| X = 3.488 + \frac{986.4}{T} + 0.01009 \, MW_g |
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| Y = 2.447 - 0.2224 \, X |
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where
fluid temperature in fluid in | ...
The model range and statistical metrics:
See also
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Petroleum Industry / Upstream / Subsurface E&P Disciplines / Fluid (PVT) Analysis / Fluid (PVT) modelling / Dynamic fluid viscosity / Dynamic fluid viscosity @model
Natural Science / Physics /Thermodynamics / Natural gas viscosity correlations
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