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Implicit Z-factor Correlations @model for the natural gas in the wide range of pseudo-reduced temperature  1.0 < T_{pr} \leq 3.0 and pseudo-reduced pressure  0.2 \leq P_{pr} \leq 30

and also a specific range of 0.7 < T_{pr} \leq 1.0 and P_{pr} < 1.0:

(1) Z = \frac{0.27 \, P_{pr}}{y \, T_{pr}}
(2) 1 + T_1 \, y +T_2 \, y^2 + T_3 \, y^5 + T_4 \, y^2 \, (1+ A_8 \, y^2) \cdot \exp \left( - A_8 \, y^2 \right) - \frac{T_5}{y} = 0


(3) T_1 = A_1 + \frac{A_2 }{ T_{pr} } + \frac{A_3 }{ T_{pr}^3 }
(4) T_2 = A_4 + \frac{A_5 }{ T_{pr} }
(5) T_3 = \frac{A_5 \, A_6 }{T_{pr}}
(6) T_4 = \frac{A_7 }{T_{pr}^3}
(7) T_5 = \frac{0.27 \, P_{pr} }{T_{pr}}

where

Z

Z-factor

T

fluid temperature 

T_{pr} = T/T_{pc}

pseudo-reduced temperature 
(or reduced temperature  T_{r} in case of pure substances)

T_{pc}

 pseudo-critical temperature 
(or critical temperature  T_{c} in case of pure substances)

P

fluid pressure

P_{pr} = P/P_{pc}

pseudo-reduced pressure 
(or reduced pressure  P_{r} in case of pure substances)

P_{pc}

 pseudo-critical pressure 
(or critical pressure  P_{c} in case of pure substances)

and

A_1 = 0.31506237

A_2 = -1.0467099

A_3 = -0.57832729

A_4 = 0.53530771

A_5 = -0.61232032

A_6 = -0.10488813

A_7 = 0.68157001

A_8 = 0.68446549

See also


Natural Science / Physics /Thermodynamics / Natural Gas Viscosity / Z-factor Correlations @model

Reference


Lee, A. L., Gonzalez, M. H., & Eakin, B. E. (1966). The Viscosity of Natural Gases. Journal of Petroleum Technology, 18(08), 997–1000. doi:10.2118/1340-PA (https://doi.org/10.2118/1340-PA)


 








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