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24-Pet-A3 Fundamental Reservoir Engineering · December 2018

Question 4 of 7: Steady-State Core Flood — Effective and Relative Permeability

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

Notes on this paper

17-Pet-A3 — Fundamental Reservoir Engineering · National Exams, December 2018 · 3 hours, closed book, approved Casio/Sharp 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: Craft, B.C. & Hawkins, M.F., Applied Petroleum Reservoir Engineering, 3rd ed. (material balance, well testing, relative permeability, Darcy flow); Ahmed, T., Reservoir Engineering Handbook, 5th ed. (material balance, transient well testing, gas PVT, decline-curve analysis); Lyons, W.C. (ed.), Standard Handbook of Petroleum and Natural Gas Engineering, 3rd ed.; McCain, W.D., The Properties of Petroleum Fluids, 3rd ed. (PVT properties, Z-factor correlations).

Question 4: Steady-State Core Flood — Effective and Relative Permeability (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. $L=10$ cm, $A=5\ \text{cm}^2$, $k_{abs}=0.5$ Darcy, $\mu_o=3.52$ cp, $\mu_w=1$ cp; steady-state co-flood rates vs. $S_w$ above (each column run at the SAME fixed differential pressure, a standard steady-state relative-permeability procedure).

Find. $k_{eff,w}$, $k_{eff,o}$, $k_{rw}$, $k_{ro}$ at $S_w=0.40$, and the inlet–outlet pressure difference at that saturation.

Approach. Use the two single-phase end points ($S_w=0$: 100% oil; $S_w=1$: 100% water) with Darcy's law and the GIVEN $k_{abs}$ to back out the common differential pressure $\Delta p$ used throughout the flood; then apply the same Darcy equation to each phase's rate at $S_w=0.40$ to get $k_{eff,w}$ and $k_{eff,o}$, and normalize by $k_{abs}$ for the relative permeabilities.

  1. Differential pressure from the single-phase end points. Darcy's law in Darcy units, $q=\dfrac{kA\Delta p}{\mu L}$. At $S_w=0$ (100% oil, $q_o=0.0780$): $\Delta p=\dfrac{q_o\mu_oL}{k_{abs}A}=\dfrac{0.0780(3.52)(10)}{0.5(5)}$, giving $\Delta p=1.098$ atm. At $S_w=1$ (100% water, $q_w=0.2750$): $\Delta p=\dfrac{0.2750(1)(10)}{0.5(5)}=1.100$ atm. The two endpoints agree, confirming a single fixed $\Delta p$ was used throughout the test: $\boxed{\Delta p=1.10\ \text{atm}}$ (average of the two).
  2. Effective permeabilities at $S_w=0.40$. Rates there: $q_w=0.0220$, $q_o=0.0260$ mL/s. $k_{eff,w}=\dfrac{q_w\mu_wL}{A\Delta p}=\dfrac{0.0220(1)(10)}{5(1.10)}$, so $\boxed{k_{eff,w}=0.0400\ \text{D}}$. $k_{eff,o}=\dfrac{q_o\mu_oL}{A\Delta p}=\dfrac{0.0260(3.52)(10)}{5(1.10)}$, so $\boxed{k_{eff,o}=0.1665\ \text{D}}$.
  3. Relative permeabilities. $k_{rw}=k_{eff,w}/k_{abs}=0.0400/0.5$, so $\boxed{k_{rw}=0.080}$. $k_{ro}=k_{eff,o}/k_{abs}=0.1665/0.5$, so $\boxed{k_{ro}=0.333}$.
  4. Inlet–outlet pressure difference at $S_w=0.40$. The differential pressure was fixed throughout the flood (Step 1), so $\boxed{\Delta p=1.10\ \text{atm}\ (\approx16.2\ \text{psi})}$ at $S_w=0.40$ as well.
Check: taking $\Delta p$ as constant across the whole flood is confirmed, not assumed — the two independent single-phase end points (Sw=0 and Sw=1) both back out $\Delta p\approx1.10$ atm from the given $k_{abs}=0.5$ D, so the two-phase rates at every intermediate saturation were clearly measured at that same fixed differential pressure.
QuantityValue
Fixed differential pressure, $\Delta p$1.10 atm
Water effective permeability, $k_{eff,w}$ (at $S_w=0.4$)0.0400 D (40.0 mD)
Oil effective permeability, $k_{eff,o}$ (at $S_w=0.4$)0.1665 D (166.5 mD)
Water relative permeability, $k_{rw}$0.080
Oil relative permeability, $k_{ro}$0.333