24-Pet-A3 Fundamental Reservoir Engineering · December 2015
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
98-Pet-A3 — Fundamental Reservoir Engineering · National Exams, December 2015 · 3 hours, closed book, non-communicating 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. All seven questions are solved below for completeness.
Reference texts: Ahmed, T., Reservoir Engineering Handbook, 5th ed. (Darcy's law and relative permeability, transient well testing, p/Z and oil material balance, capillary pressure); Craft, B.C. & Hawkins, M.F., Applied Petroleum Reservoir Engineering, 3rd ed. (reservoir drive mechanisms, pseudo-steady-state inflow); Lyons, W.C. (ed.), Standard Handbook of Petroleum and Natural Gas Engineering, 3rd ed. (Standing–Katz Z-factor correlation, Dranchuk–Abu-Kassem fit); McCain, W.D., The Properties of Petroleum Fluids, 3rd ed. (capillary pressure and relative permeability laboratory data).
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.
| Gas specific gravity, $\gamma_g$ | 0.65 (air = 1) |
| Initial pressure, $p_i$ | 4000 psia |
| Formation temperature, $T$ | 200°F = 660°R |
| Cumulative production at $p_1=3000$ psia, $G_{p1}$ | 500 MMSCF |
| Target pressure, $p_2$ | 2000 psia |
Find. The original gas in place $G$, and the cumulative gas production $G_{p2}$ when $p$ drops to 2000 psia.
Approach. Compute pseudo-critical properties from $\gamma_g$, get $T_{pr}$ and $P_{pr}$ at each pressure, solve for $Z$ via the DAK correlation, then fit the two known $(G_p,\,p/Z)$ points to the straight-line volumetric gas material balance $p/Z=(p_i/Z_i)(1-G_p/G)$ to get $G$, and evaluate it again at $p_2$.
| Quantity | Value |
|---|---|
| $T_{pc}$, $P_{pc}$ | 374.0 °R, 670.9 psia |
| $Z_i$, $Z_1$, $Z_2$ | 0.9350, 0.8925, 0.8860 |
| Original gas in place, $G$ | 2333 MMSCF (2.33 Bscf) |
| Cumulative production at $p=2000$ psia, $G_{p2}$ | 1102 MMSCF |