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24-Pet-A2 Petroleum Reservoir Fluids · December 2018

Question 4 of 7: Two-Phase PVT Cell — n-Decane / Ethane Flash

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 4: Two-Phase PVT Cell — n-Decane / Ethane Flash (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.

Given.

QuantityValue
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 $y_i=K_ix_i$.

  1. Set up the flash equation. With $V=0.10$: for n-decane, $1+V(K_{C_{10}}-1)=1+0.10(0.005-1)=0.9005$; for ethane, $1+V(K_{C_2}-1)=1+0.10(8-1)=1.700$. The flash constraint is $\dfrac{z_{C_{10}}}{0.9005}+\dfrac{z_{C_2}}{1.700}=1$.
  2. Part (a) — solve for moles of ethane. Substituting $z_{C_{10}}=1/(1+x)$, $z_{C_2}=x/(1+x)$ and multiplying through by $(1+x)$: $\dfrac{1}{0.9005}+\dfrac{x}{1.700}=1+x$. Rearranging, $\left(\dfrac{1}{0.9005}-1\right)=x\left(1-\dfrac{1}{1.700}\right)$, i.e. $0.11049=0.41176\,x$, so $\boxed{x=n_{C_2}\approx0.268\ \text{mol}}$ of ethane.
  3. Part (b) — overall and phase compositions. Total moles $=1+0.268=1.268$, giving overall mole fractions $z_{C_{10}}=1/1.268=0.7884$ and $z_{C_2}=0.268/1.268=0.2116$. Liquid-phase compositions: $x_{C_{10}}=z_{C_{10}}/0.9005=0.7884/0.9005$, so $\boxed{x_{C_{10}}\approx0.8755}$; $x_{C_2}=z_{C_2}/1.700=0.2116/1.700$, so $\boxed{x_{C_2}\approx0.1245}$ (sum $=1.000$, checks). Vapour-phase compositions from $y_i=K_ix_i$: $y_{C_{10}}=0.005\times0.8755$, so $\boxed{y_{C_{10}}\approx0.0044}$; $y_{C_2}=8\times0.1245$, so $\boxed{y_{C_2}\approx0.9956}$ (sum $=1.000$, checks).
QuantityValue
(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