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24-Pet-A2 Petroleum Reservoir Fluids · May 2018

Question 7 of 7: Real-Gas Formation Volume Factor and Density via the Standing–Katz Chart

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

Notes on this paper

17-Pet-A2 — Petroleum Reservoir Fluids · National Exams, May 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, gas hydrates/waxes/asphaltenes); Ahmed, T., Reservoir Engineering Handbook, 5th ed. (material balance, well-stream gravity, pseudo-critical property correlations); Danesh, A., PVT and Phase Behaviour of Petroleum Reservoir Fluids (equilibrium K-value flash calculations, Gibbs' phase rule).

Question 7: Real-Gas Formation Volume Factor and Density via the Standing–Katz Chart (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.

Check: this question reuses the same 7-component separator-gas composition and molecular weights given in Question 6's table (Methane 71%, Ethane 10%, Propane 9%, i-Butane 3%, n-Butane 4%, i-Pentane 2%, n-Pentane 1%) — the source paper prints the identical table a second time on this page rather than cross-referencing it.

Given. Gas-phase composition (as in Question 6); $p=4000$ psia; $T=180\,{}^{\circ}\text{F}$; $MW_{air}=28.97\ \text{lb}_{mass}/\text{lb-mole}$; formula sheet: $T_{pc}=168+325\gamma_g-12.5\gamma_g^2$ (°R), $p_{pc}=677+15.0\gamma_g-37.5\gamma_g^2$ (psia), $B_g=0.02827\dfrac{ZT}{p}$ (ft$^3$/SCF), $\rho=\dfrac{pMW}{ZRT}$ with $R=10.732\ \text{psi-ft}^3/(\text{lb-mole-}{}^{\circ}\text{R})$.

Find. $B_g$ (ft$^3$/SCF) and gas density $\rho$ (lb$_{mass}$/ft$^3$) at the stated conditions.

Approach. Compute the gas's average molecular weight and specific gravity from its composition, use the formula-sheet correlations to get pseudo-critical properties (and hence $T_r$, $p_r$), read the compressibility factor $Z$ off the Standing–Katz chart at that $(T_r,p_r)$, then substitute into the $B_g$ and $\rho$ formulas.

  1. Average molecular weight and gas gravity. $MW_{avg}=\sum y_iMW_i=24.60\ \text{lb}_{mass}/\text{lb-mole}$ (same composition and calculation as Question 6's gas phase). $\gamma_g=\dfrac{MW_{avg}}{MW_{air}}=\dfrac{24.60}{28.97}$, so $\boxed{\gamma_g\approx0.849}$.
  2. Pseudo-critical properties. $T_{pc}=168+325(0.849)-12.5(0.849)^2=168+276.1-9.01$, so $\boxed{T_{pc}\approx434.96\,{}^{\circ}\text{R}}$. $p_{pc}=677+15.0(0.849)-37.5(0.849)^2=677+12.73-27.03$, so $\boxed{p_{pc}\approx662.70\ \text{psia}}$.
  3. Reduced temperature and pressure. $T=180\,{}^{\circ}\text{F}=180+459.67=639.67\,{}^{\circ}\text{R}$. $T_r=\dfrac{T}{T_{pc}}=\dfrac{639.67}{434.96}$, so $\boxed{T_r\approx1.47}$. $p_r=\dfrac{p}{p_{pc}}=\dfrac{4000}{662.70}$, so $\boxed{p_r\approx6.04}$.
  4. Compressibility factor from the Standing–Katz chart. Locating $(p_r,T_r)=(6.04,1.47)$ on the chart (Question 1's formula-sheet page reproduces this same chart) lands on the $T_r\approx1.45$–$1.5$ curve family in its high-pressure, low-$Z$ trough: $\boxed{Z\approx0.85}$.
  5. Gas formation volume factor. $B_g=0.02827\dfrac{ZT}{p}=0.02827\times\dfrac{0.854\times639.67}{4000}$, so $\boxed{B_g\approx0.00386\ \text{ft}^3/\text{SCF}}$.
  6. Gas density. $\rho=\dfrac{pMW_{avg}}{ZRT}=\dfrac{4000\times24.60}{0.854\times10.732\times639.67}$, so $\boxed{\rho\approx16.8\ \text{lb}_{mass}/\text{ft}^3}$ — roughly 22 times denser than the same gas at standard conditions ($\rho_{sc}=MW_{avg}/379.4\approx0.065\ \text{lb}_{mass}/\text{ft}^3$), reflecting the very high reservoir pressure.
Pseudo-reduced pressure, p_r Compressibility factor, Z 0 7 15 0.6 1.0 1.4 T_r = 2.0 T_r = 1.7 T_r = 1.45-1.5 (this gas) T_r = 1.2 (p_r, T_r) = (6.04, 1.47) → Z ≈ 0.85
Schematic Standing–Katz $Z$-factor chart (see the formula-sheet page for the full chart): the query point at $p_r=6.04$, $T_r=1.47$ falls in the low-$Z$ trough characteristic of moderately reduced temperatures at high reduced pressure, reading $Z\approx0.85$.
QuantityValue
Average molecular weight, $MW_{avg}$24.60 lb$_{mass}$/lb-mole
Gas specific gravity, $\gamma_g$0.849
$T_{pc}$ / $p_{pc}$434.96 °R / 662.70 psia
$T_r$ / $p_r$1.47 / 6.04
Compressibility factor, $Z$≈0.85
Gas formation volume factor, $B_g$0.00386 ft$^3$/SCF
Gas density, $\rho$16.8 lb$_{mass}$/ft$^3$
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