24-Pet-A2 Petroleum Reservoir Fluids · December 2014
Question 4 of 7: Bubble Point and Formation Volume Factors from PVT Data
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
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 4: Bubble Point and Formation Volume Factors from PVT Data (20 marks)
Given. The PVT table above; formula sheet relations $B_t=B_o+B_g(R_{sob}-R_{so})$ and $c=-\dfrac{1}{B_{ob}}\left(\dfrac{dB_o}{dP}\right)_T$; unit conversion 1 bbl $=5.615\ \text{ft}^3$.
Find. (a) bubble-point pressure $p_b$; (b) $B_t$ at $p_b$; (c) isothermal oil compressibility at 4000 psia; (d) $B_t$ at 2000 psia.
Approach. Locate $p_b$ as the pressure at which $R_s$ stops declining (all gas still in solution) and $B_o$ is at its maximum; apply the two-phase FVF formula at and below $p_b$, converting the table's $B_g$ from ft$^3$/SCF to bbl/SCF so it is dimensionally consistent with $B_o$; estimate the compressibility slope from the bracketing table points.
Part (a) — Bubble point. Reading down the table, $R_s$ is constant at 950 SCF/STB for $p=4500,4000,3500$ psia and then drops to 810 SCF/STB at 3000 psia — free gas can only appear once $p$ drops below $p_b$, so $p_b$ is the lowest pressure at which $R_s$ is still at its plateau value. This is confirmed by $B_o$: it rises with declining pressure above $p_b$ (pure liquid expansion: 1.31→1.32→1.33) and only turns over and falls once gas begins evolving (1.33→1.30). The peak $B_o=1.33$ bbl/STB at $p=3500$ psia locates $\boxed{p_b = 3500\ \text{psia}}$.
Part (b) — $B_t$ at bubble point. At $p_b$ the oil is exactly saturated, so $R_{so}=R_{sob}=950$ SCF/STB and the free-gas term vanishes: $B_t=B_o+B_g(R_{sob}-R_{so})=1.33+B_g(0)$. So $\boxed{B_t(p_b) = 1.33\ \text{bbl/STB}}$ — at the bubble point the total and oil FVF are identical, by definition.
Part (c) — Compressibility at 4000 psia. 4000 psia sits between the two undersaturated table points 4500 psia ($B_o=1.31$) and 3500 psia ($B_o=1.33$); estimate the slope by central difference: $\left(\dfrac{dB_o}{dP}\right)_T \approx \dfrac{1.33-1.31}{3500-4500}=\dfrac{0.02}{-1000}=-2.0\times10^{-5}\ \text{bbl/STB per psi}$. Using $B_{ob}=1.33$ bbl/STB from Part (b): $c=-\dfrac{1}{1.33}\times(-2.0\times10^{-5})$, giving $\boxed{c = 1.50\times10^{-5}\ \text{psi}^{-1}}$ at 4000 psia.
Part (d) — $B_t$ at 2000 psia. Below $p_b$: $B_o(2000)=1.23$ bbl/STB, $R_{so}(2000)=550$ SCF/STB, $B_g(2000)=0.0070185\ \text{ft}^3/\text{SCF}$. Convert $B_g$ to bbl/SCF: $B_g=0.0070185/5.615=0.0012500\ \text{bbl/SCF}$. Then $B_t=B_o+B_g(R_{sob}-R_{so})=1.23+0.0012500\times(950-550)=1.23+0.0012500\times400=1.23+0.500$. So $\boxed{B_t(2000\ \text{psia}) = 1.730\ \text{bbl/STB}}$.