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Implicit Z-factor Correlations @model for the natural gas in the wide range of pseudo-reduced temperature  1.05 \leq T_{pr} \leq 3 and pseudo-reduced pressure  0.2 \leq P_{pr} \leq 15:

(1) Z = \frac{0.27 \, P_{pr}}{y \, T_{pr}}
(2) R_5 \, y^2 \, (1+ A_{11} \, y^2) \cdot \exp \left( - A_{11} \, y^2 \right) + R_1 \, y - \frac{R_2}{y} +R_3 \, y^2 - R_4 \, y^5 +1 = 0
(3) R_1 = A_1 + A_2 \, t + A_3 \, t^3 + A_4 \, t^4 + A_5 \, t^5
(4) R_2 = \frac{0.27 \, P_{pr}}{T_{pr}}
(5) R_3 = A_6 + A_7 \, t + A_8 \, t^2



(6) R_4 = A_9 \, ( A_7 \, t + A_8 \, t^2)
(7) R_5 = A_10 \, t^3



(8) t= \frac{1}{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 = 0.3265

A_2 = -1.070

A_3 = - 0.5339

A_4 = 0.01569

A_5 = - 0.05165

A_6 = 0.5475

A_7 = 0.7361

A_8 = 0.1844

A_9 = 0.1056

A_{10} = 0.6134

A_{11} = 0.7210











See also


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

Reference


Dranchuk, P.M., and H. Abou-Kassem. "Calculation of Z Factors For Natural Gases Using Equations of State." J Can Pet Technol 14 (1975): doi.org/10.2118/75-03-03

Lateef A. Kareem, et al, New explicit correlation for the compressibility factor of natural gas: linearized z-factor isotherms, J Petrol Explor Prod Technol (2016) 6:481–492, DOI 10.1007/s13202-015-0209-3

 






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