24-Pet-A2 Petroleum Reservoir Fluids · December 2014
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
98-Pet-A2 — Petroleum Reservoir Fluids · National Exams, December 2014 · 3 hours, closed book, Casio/Sharp approved calculator only · first five questions in the answer book are marked, all questions equal value.
Reference texts: Craft, B.C. & Hawkins, M.F., Applied Petroleum Reservoir Engineering, 3rd ed. (Ch. 1–2, PVT properties of oil, gas and gas-condensate systems); Lyons, W.C. (ed.), Standard Handbook of Petroleum and Natural Gas Engineering, 3rd ed. (reservoir fluid properties, Standing-Katz Z-factor correlation); McCain, W.D., The Properties of Petroleum Fluids (companion reference for laboratory PVT experiments and recombination calculations, cited within Craft & Hawkins Ch. 1).
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. Feed $z_A=0.40$, $z_B=0.60$; $K_A=10$, $K_B=0.04$ at cell conditions (500 psia, 100°F). Formula sheet: Rachford–Rice $\sum_i \dfrac{z_i(K_i-1)}{1+V(K_i-1)}=0$, $x_i=\dfrac{z_i}{1+V(K_i-1)}$, $y_i=K_ix_i$, $L+V=1$.
Find. Vapour fraction $V$, liquid fraction $L$, and phase compositions $x_A,x_B,y_A,y_B$.
Approach. Solve the two-component Rachford–Rice objective function for $V$ directly (it reduces to one linear equation for a binary system), then back out phase compositions from the flash relations.
| Quantity | Value |
|---|---|
| Vapour fraction $V$ | 0.350 |
| Liquid fraction $L$ | 0.650 |
| $x_A$, $x_B$ (liquid) | 0.0964, 0.9036 |
| $y_A$, $y_B$ (vapour) | 0.9639, 0.0361 |