Horizontal Well Technology

The ideal-gas law states that the behavior of a gas can be expressed as
where
p = Pressure, psia
V = Volume, ft 3
n = Number of moles
R = The gas constant, ft 3-psi/( R-lb-moles)
T = Temperature, Rankine ( R)
As shown below, the ideal-gas law, Equation B-1, can be modified to account for deviation of a real gas from ideal-gas behavior.
where z is compressibility factor. The Theorem of Corresponding States demonstrates that real gas mixtures will have the same z- factor for the same values of pseudo-reduced pressure p pr and pseudo-reduced temperature T pr which are defined as
where p pc and T pc are the pseudo-critical pressure and temperature for hydrocarbon gases, respectively. Table B-1 lists p pc and T pc as a function of gas gravity ? g for values of ? g ranging from 0.55 to 1.14. [1] Figure A-8 is Standing and Katz chart for determining z-factors for natural gases as a function of pseudo-reduced pressure p pr and temperature T pr. [2]
| ? g | P pc | T pc | ? g | P pc | T pc |
|---|---|---|---|---|---|
| 0.55 | 673 | 336 | 0.85 | 664 | 441 |
| 0.56 | 673 | 341 | 0.86 | 664 | 444 |
| 0.57 | 672 | 346 | 0.87 | 663 | 448 |
| 0.58 | 672 | 350 | 0.88 | 663 | 451 |
| 0.59 | 672 | 354 | 0.89 | 662 | 454 |
| 0.60 | 671 | 358 | 0.90 | 662 |