Difference between revisions of "P/Z plot"
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The [[P/Z plot]] is based on the [[Gas Material Balance]] equation. | The [[P/Z plot]] is based on the [[Gas Material Balance]] equation. | ||
− | :<math> | + | Applying [[Real gas]] [[EOS]] at reservoir conditions: |
+ | (1):<math> PV_r=z\frac{m}{M} RT_r</math> | ||
+ | |||
+ | Applying [[Real gas]] [[EOS]] at standard conditions: | ||
+ | (2):<math> P_{SC}V_g=1\frac{m}{M} RT_{SC}</math> | ||
+ | |||
+ | Dividing eq (2) by eq (1) and rearranging: | ||
+ | (3):<math> V_g=\frac{P}{z} \frac{V_rT_{SC}}{P_{SC}T_{r}}</math> | ||
− | |||
− | |||
:<math> V_g=\frac{P}{z}\frac{V_rT_{SC}}{P_{SC}T_r}</math> (3) | :<math> V_g=\frac{P}{z}\frac{V_rT_{SC}}{P_{SC}T_r}</math> (3) |
Revision as of 08:49, 21 November 2017
Brief
The P/Z plot is a plot of P/Z versus cumulative gas production, Gp.
The interpretation technique is fitting the data points with the straight line to estimate GIIP.
Math & Physics
The P/Z plot is based on the Gas Material Balance equation.
Applying Real gas EOS at reservoir conditions: (1):
Applying Real gas EOS at standard conditions: (2):
Dividing eq (2) by eq (1) and rearranging: (3):
- (3)
The bubble flow exist when:
- , with the limit [2]
The gas holdup:
Discussion
Griffith correlation adds a hook to the originally straight Hagedorn and Brown VLP curve.
Nomenclature
- = pipe diameter, ft
- = gas holdup factor, dimensionless
- = bubble-slug boundary, dimensionless
- = gas velocity, ft/sec
- = liquid velocity, ft/sec
- = 0.8, slip velocity (difference between average gas and liquid velocities), ft/sec
References
- ↑ Economides, M.J.; Hill, A.D.; Economides, C.E.; Zhu, D. (2013). Petroleum Production Systems (2 ed.). Westford, Massachusetts: Prentice Hall. ISBN 978-0-13-703158-0.
- ↑ 2.0 2.1 Orkiszewski, J. (June 1967). "Predicting Two-Phase Pressure Drops in Vertical Pipe". Journal of Petroleum Technology. SPE. 19 (SPE-1546-PA).
Cite error: <ref>
tag with name "Griffith" defined in <references>
is not used in prior text.