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24-Pet-A3 Fundamental Reservoir Engineering · December 2014

Question 4 of 7: Volumetric Gas Reservoir — p/Z Material Balance

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

98-Pet-A3 — Fundamental Reservoir Engineering · National Exams, December 2014 · 3 hours, closed book, Casio/Sharp approved calculator only · five (5) questions constitute a complete exam paper (the first five as they appear in the answer book are marked), all questions equal value, all parts of a multipart question equal weight.

Reference texts: Ahmed, T., Reservoir Engineering Handbook, 5th ed. (Darcy's law and fluid potential, transient well testing, p/Z and oil material balance, capillary pressure/relative permeability); Craft, B.C. & Hawkins, M.F., Applied Petroleum Reservoir Engineering, 3rd ed. (reservoir drive mechanisms, material balance fundamentals); Lyons, W.C. (ed.), Standard Handbook of Petroleum and Natural Gas Engineering, 3rd ed. (Standing–Katz Z-factor correlation); McCain, W.D., The Properties of Petroleum Fluids, 3rd ed. (capillary pressure and relative permeability laboratory data).

Question 4: Volumetric Gas Reservoir — p/Z Material Balance (20 marks)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Check: the paper labels cumulative production "MMMSCF" (triple-M); this reads as a misprint of the standard "MMSCF" (10$^6$ SCF) unit, but since parts (a) and (b) below both reduce to a ratio $G_p/G$, the numeric answer is unaffected by which reading is intended — the unit label is carried through as printed.

Given. $\gamma_g=0.67$; $T=237\,{}^{\circ}\text{F}=697\,{}^{\circ}\text{R}$ (constant); two ($p$, $G_p$) data pairs above. Formula sheet: $T_{pc}=168+325\gamma_g-12.5\gamma_g^2$, $p_{pc}=677+15.0\gamma_g-37.5\gamma_g^2$; $p/Z=(p_i/Z_i)(1-G_p/G)$.

Find. (a) Initial gas in place, $G$; (b) recovery factor at $p=500$ psia.

03005209001200150017650100020003000400050005959Cumulative gas production, Gp (MMMSCF)p/Z (psia)G = 1765 MMMSCF
Fig. 3 — The two ($G_p$, $p/Z$) points define a straight line; its $G_p$-intercept is the initial gas in place $G$.

Approach. Build pseudo-critical properties from $\gamma_g$, form $Z$ at each tabulated pressure via the Standing–Katz correlation, plot $p/Z$ against $G_p$, and fit the straight line $p/Z=(p_i/Z_i)-(p_i/Z_i)/G\cdot G_p$ through the two points to solve simultaneously for the intercept and $G$; apply the same relation at 500 psia for part (b).

  1. Pseudo-critical properties. $T_{pc}=168+325(0.67)-12.5(0.67)^2=380.1\,{}^{\circ}\text{R}$; $p_{pc}=677+15.0(0.67)-37.5(0.67)^2=670.2$ psia; $T_r=697/380.1=\boxed{1.834}$ (constant for this isothermal reservoir).
  2. $Z$ and $p/Z$ at the two data points. At $p=5000$: $p_r=7.460$, Standing–Katz gives $Z=1.011$, so $p/Z=4946$ psia. At $p=4000$: $p_r=5.968$, $Z=0.952$, $p/Z=4203$ psia.
  3. Fit the line and solve for $G$. Slope $=\dfrac{4203-4946}{520-300}=-3.376$ psia/MMMSCF; intercept $p_i/Z_i=4946-(-3.376)(300)=5959$ psia. $\boxed{G=5959/3.376=1765\ \text{MMMSCF}}$.
  4. Recovery factor at 500 psia. $p_r=500/670.2=0.746$, $Z=0.965$, $p/Z=518.3$ psia. $G_p(500)=(5959-518.3)/3.376=1611.5$ MMMSCF. $\boxed{\text{RF}=1611.5/1765=91.3\%}$.
QuantityValue
$T_r$ (constant)1.834
(a) Initial gas in place, $G$1765 MMMSCF
(b) $G_p$ at 500 psia1611.5 MMMSCF
(b) Recovery factor at 500 psia91.3%