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24-Pet-A2 Petroleum Reservoir Fluids · December 2018

Question 6 of 7: Schematic Black-Oil PVT Property Trends vs. Pressure

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

Notes on this paper

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 6: Schematic Black-Oil PVT Property Trends vs. Pressure (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.

Approach. All five properties are governed by the same physical picture: above the bubble point $p_b$ the oil is a single-phase undersaturated liquid holding a fixed dissolved-gas content $R_{sob}$, so its behaviour is that of an ordinary (weakly compressible) liquid; below $p_b$ gas evolves out of solution as pressure falls, and every property's trend changes character exactly at $p_b$. Each panel below marks $p_b$ with a dashed vertical line.

p_b (a) Oil viscosity, μo μo pressure, p → undersaturated saturated p_b (b) Oil FVF, Bo Bo pressure, p → Bob (max) p_b (c) Total FVF, Bt Bt pressure, p → Bt = Bo + Bg(Rsob-Rso) Bt = Bo above p_b p_b (d) Solution GOR, Rso Rso pressure, p → constant = Rsob p_b (e) Oil compressibility, co co pressure, p → defined above p_b only two-phase system near p_b
Schematic black-oil PVT property trends vs. pressure at constant reservoir temperature, bubble point $p_b$ marked with a dashed line on every panel. (a) $\mu_o$ falls as pressure declines toward $p_b$ (more dissolved gas thins the oil), reaching a minimum exactly at $p_b$, then rises again below $p_b$ as the oil loses light ends to the evolving gas. (b) $B_o$ rises from 1 (surface) up to a maximum $B_{ob}$ at $p_b$ as more gas dissolves with increasing pressure below $p_b$, then falls slightly above $p_b$ as the single-phase liquid is isothermally compressed. (c) $B_t=B_o+B_g(R_{sob}-R_{so})$ coincides with $B_o$ above $p_b$ (no free gas, $R_{so}=R_{sob}$) but diverges sharply upward below $p_b$ as the evolved free-gas volume $B_g$ grows rapidly with falling pressure. (d) $R_{so}$ rises with pressure below $p_b$ as more gas dissolves, then is CONSTANT (=$R_{sob}$) above $p_b$, since no more gas is available to dissolve into an already-saturated oil. (e) $c_o$ is defined only above $p_b$ (single-phase liquid), decreasing mildly as pressure rises further above $p_b$; approaching $p_b$ from above it, and immediately below it, the system's effective compressibility rises sharply because the free gas phase near saturation is far more compressible than the liquid alone.
PropertyTrend vs. pressure (constant T)
(a) $\mu_o$Falls to a minimum at $p_b$, then rises below $p_b$
(b) $B_o$Rises to a maximum $B_{ob}$ at $p_b$, then falls slightly above $p_b$
(c) $B_t$Equals $B_o$ above $p_b$; diverges upward sharply below $p_b$
(d) $R_{so}$Rises with $p$ below $p_b$; constant $=R_{sob}$ above $p_b$
(e) $c_o$Defined only above $p_b$; decreases mildly with increasing $p$, spikes approaching $p_b$