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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) T_4 \, y^2 \, (1+ A_8 \, y^2) \cdot \exp \left( - A_8 \, y^2 \right) +1 + T_1 \, y +T_2 \, y^2 + T_3 \, y^5 + \frac{T_5}{y} = 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 \cdot ( 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., Purvis, R.A., and D.B. Robinson. "Computer Calculation Of Natural Gas Compressibility Factors Using The Standing And Katz Correlation." Paper presented at the Annual Technical Meeting, Edmonton, May 1973. doi: https://doi.org/10.2118/73-112

https://rdrr.io/github/f0nzie/zFactor/man/Dranchuk-Purvis-Robinson.html

 








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