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24-Pet-A3 Fundamental Reservoir Engineering · December 2014

Question 7 of 7: Dry Gas Reservoir — Depletion and Gas Produced

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 7: Dry Gas Reservoir — Depletion and Gas Produced (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.

Given.

Initial pressure, $p_i$6000 psia
Reservoir temperature, $T$160 °F = 620 °R
Gas gravity, $\gamma_g$0.65
Original reservoir gas volume1 MMft$^3$ (given for the second part)
Final pressure (second part)500 psia

Find. (i) The average reservoir pressure at 50% recovery ($G_p/G=0.5$); (ii) the volume of gas produced (SCF) when the reservoir depletes from $p_i$ to 500 psia, given the reservoir originally held 1 MMft$^3$ of reservoir-condition gas.

Approach. Build the pseudo-critical properties and $Z_i$ at $p_i$, then use the volumetric $p/Z=(p_i/Z_i)(1-G_p/G)$ relation: for (i), solve for the pressure at which $G_p/G=0.5$ (iteratively, since $Z$ itself depends on $p$); for (ii), convert the given 1 MMft$^3$ reservoir volume to gas-in-place $G$ (SCF) via $B_{gi}$, then apply the same relation at $p_f=500$ psia to get $G_p$.

  1. Pseudo-criticals and $Z_i$. $T_{pc}=168+325(0.65)-12.5(0.65)^2=374.0\,{}^{\circ}\text{R}$; $p_{pc}=677+15.0(0.65)-37.5(0.65)^2=670.9$ psia; $T_r=620/374.0=1.658$. At $p_i=6000$: $p_r=8.943$, Standing–Katz gives $\boxed{Z_i=1.064}$, so $p_i/Z_i=6000/1.064=5637$ psia.
  2. Pressure at 50% recovery. Require $p/Z=0.5(5637)=2818.5$ psia. Solving $p/Z(p)=2818.5$ iteratively (with $Z$ from the same correlation at each trial $p_r$) gives $\boxed{p=2385\ \text{psia}}$ (at which $Z=0.846$).
  3. Gas in place from reservoir volume. $B_{gi}=0.02827\dfrac{Z_iT}{p_i}=0.02827\dfrac{(1.064)(620)}{6000}=0.003109$ ft$^3$/SCF. $\boxed{G=\dfrac{1{,}000{,}000}{0.003109}=321.6\ \text{MMSCF}}$.
  4. Gas produced at $p_f=500$ psia. $p_r=500/670.9=0.745$, $Z_f=0.949$, $p_f/Z_f=526.9$ psia. $G_p=G\left(1-\dfrac{p_f/Z_f}{p_i/Z_i}\right)=321.6\left(1-\dfrac{526.9}{5637}\right)=321.6(0.9065)$, so $\boxed{G_p=291.5\ \text{MMSCF}}$.
QuantityValue
$Z_i$ at 6000 psia1.064
(i) Pressure at 50% recovery2385 psia
Initial gas in place, $G$ (from 1 MMft$^3$)321.6 MMSCF
(ii) Gas produced at 500 psia291.5 MMSCF
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