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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{A_1 \, P_{pr}}{y}
(2) -A_1 \, P_{pr} + \frac{y+y^2+y^3-y^4}{(1-y)^3} - A_2 \, y^2 + A_3 \, y^{\, A_4} = 0
(3) A_1 = 0.06125 \cdot t \cdot \exp \left[ -1.2 (1-t)^2 \right]
(4) A_2 = 14.76 \, t - 9.76 \, t^2 +4.58 \, t^3
(5) A_3 = 90.7 \, t -242.2 \, t^2 + 42.4 \, t^3



(6) A_4 = 2.18 + 2.82 \, t
(7) 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)


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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