24-Pet-A2 Petroleum Reservoir Fluids · December 2018
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
17-Pet-A2 — Petroleum Reservoir Fluids · National Exams, December 2018 · 3 hours, closed book, Casio/Sharp approved calculators only · a formula sheet is provided; FIVE (5) questions constitute a complete exam paper (the first five as submitted are marked); all questions equal value, all parts of a multipart question equal weight; oilfield-unit questions must be answered in field units.
Reference texts: Craft, B.C. & Hawkins, M.F., Applied Petroleum Reservoir Engineering, 3rd ed. (Ch. 1–2, PVT properties, reservoir/well-stream classification); Lyons, W.C. (ed.), Standard Handbook of Petroleum and Natural Gas Engineering, 3rd ed. (Standing–Katz Z-factor correlation, gas properties); McCain, W.D., The Properties of Petroleum Fluids, 3rd ed. (phase behaviour, black-oil PVT laboratory data); Ahmed, T., Reservoir Engineering Handbook, 5th ed. (material balance, pseudo-critical property correlations, gas/oil PVT relations); Danesh, A., PVT and Phase Behaviour of Petroleum Reservoir Fluids (equilibrium K-value flash calculations, Gibbs' phase rule).
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.
| Quantity | Value |
|---|---|
| n-Decane charged, $n_{C_{10}}$ | 1 mol |
| Vapour fraction of the cell (mole basis), $V$ | 0.10 (10% gas) |
| Liquid fraction, $L$ | 0.90 (90% liquid) |
| K-value, n-decane, $K_{C_{10}}$ | 0.005 |
| K-value, ethane, $K_{C_2}$ | 8 |
Find. (a) Moles of ethane charged, $n_{C_2}$; (b) equilibrium liquid ($x_i$) and vapour ($y_i$) mole fractions of both components.
Approach. Let $x=n_{C_2}$ (mol). The overall mole fractions are $z_{C_{10}}=1/(1+x)$ and $z_{C_2}=x/(1+x)$. Apply the formula-sheet flash relation $\sum_i z_i/[1+V(K_i-1)]=1$ at the given $V=0.10$ to solve for $x$, then recover $x_i=z_i/[1+V(K_i-1)]$ and $y_i=K_ix_i$.
| Quantity | Value |
|---|---|
| (a) Moles of ethane charged, $n_{C_2}$ | 0.268 mol |
| (b) Liquid phase: $x_{C_{10}}$ / $x_{C_2}$ | 0.8755 / 0.1245 |
| (b) Vapour phase: $y_{C_{10}}$ / $y_{C_2}$ | 0.0044 / 0.9956 |