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24-Pet-A3 Fundamental Reservoir Engineering · May 2014

Question 5 of 7: Undersaturated-to-Saturated Oil 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, May 2014 · 3 hours, closed book, non-communicating calculator only · first five questions in the answer book are marked, all questions equal value, all parts of a multipart question equal weight. All seven questions are answered here as a complete study resource.

Reference texts: Craft, B.C. & Hawkins, M.F., Applied Petroleum Reservoir Engineering, 3rd ed. (material balance, transient well testing, radial flow); Ahmed, T., Reservoir Engineering Handbook, 5th ed. (material balance, skin/productivity, relative permeability); McCain, W.D., The Properties of Petroleum Fluids, 3rd ed. (PVT properties, Z-factor); Lyons, W.C. (ed.), Standard Handbook of Petroleum and Natural Gas Engineering, 3rd ed. (core analysis, capillary pressure).

Question 5: Undersaturated-to-Saturated Oil 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.

Given.

Pressure (psia)$B_o$ (bbl/STB)$R_{so}$ (SCF/STB)Z$B_g$ (bbl/SCF)
4000 ($p_i$)1.1810000.8500.000766
35001.2010000.7850.000706
30001.108000.7650.000860

$S_{wi}=20\%$; no initial gas cap, no water influx (volumetric, closed reservoir).

Find. (a) $N_p/N$ at bubble-point pressure; (b) current gas saturation at 3000 psia if $N_p/N=10\%$.

Approach. $R_{so}$ stays at 1000 SCF/STB from 4000 down to 3500 psia and only falls (to 800) by 3000 psia — solution gas has not yet begun evolving at 3500 psia, so the bubble point is $p_b=3500$ psia. Above $p_b$ recovery is by fluid expansion only ($N_p/N=(B_{ob}-B_{oi})/B_{ob}$); below $p_b$, use a saturation balance to convert produced oil (at the current $B_o$) into liberated gas saturation, holding connate water constant.

  1. Part (a) — recovery at the bubble point. Above $p_b$, with no free gas yet released, $N_p\,B_{ob}=N(B_{ob}-B_{oi})$ (fluid-expansion drive only), so: $$\frac{N_p}{N}=\frac{B_{ob}-B_{oi}}{B_{ob}}=\frac{1.20-1.18}{1.20}$$ giving $\boxed{N_p/N=1.67\%}$ — the small recovery typical of depletion above the bubble point, driven only by fluid expansion.
  2. Part (b) — oil saturation remaining at 3000 psia. With $N_p/N=10\%$, the remaining oil occupies a reservoir volume of $(1-N_p/N)\,N\,B_o$ against an original hydrocarbon pore volume of $N B_{oi}/(1-S_{wi})$ (holding total pore volume and $S_{wi}$ fixed, no water influx): $$S_o=(1-N_p/N)\frac{B_o}{B_{oi}}(1-S_{wi})=(0.90)\left(\frac{1.10}{1.18}\right)(0.80)=0.6712$$
  3. Current gas saturation. $S_g=1-S_{wi}-S_o=1-0.20-0.6712$, so $\boxed{S_g=12.9\%}$.
Check: assumes connate water saturation stays fixed at 20% (no water influx/production) and that no secondary gas cap has segregated updip of the well/log location by 3000 psia, so the liberated gas simply fills the pore space vacated by expanding/produced oil in place — the standard simplifying assumption for a volumetric solution-gas-drive material balance absent explicit rock/water-compressibility data.
QuantityValue
Bubble-point pressure (identified)3500 psia
(a) $N_p/N$ at bubble point1.67%
(b) Oil saturation at 3000 psia ($N_p/N=10\%$)67.1%
(b) Gas saturation at 3000 psia12.9%