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24-Pet-A7 Secondary and Enhanced Oil Recovery · May 2013

Question 1 of 4: Line-Drive Waterflood — Fractional Flow, Breakthrough Time, Saturation Profile

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

Notes on this paper

98-Pet-A7 — Secondary and Enhanced Recovery · National Exams, May 2013 · 3 hours, open-book exam, non-communicating calculator permitted · four problems, all required (the exam's own instructions mark only the first four questions as they appear in the answer book, and there are exactly four on this paper).

Reference texts: Green, D.W. & Willhite, G.P., Enhanced Oil Recovery, SPE Textbook Series Vol. 6 (waterflooding, Buckley-Leverett/Welge, polymer flooding, miscible flooding, steam flooding); Lake, L.W., Enhanced Oil Recovery, 1st ed. (fractional flow, dispersion, miscible displacement); Prats, M., Thermal Recovery, SPE Monograph Vol. 7 (steam quality, thermal front propagation); Whitson, C.H. & Brulé, M.R., Phase Behavior, SPE Monograph Vol. 20 (binary P-T diagrams, critical locus); Craft, B.C. & Hawkins, M.F., Applied Petroleum Reservoir Engineering, 3rd ed.

Problem 1: Line-Drive Waterflood — Fractional Flow, Breakthrough Time, Saturation Profile (30 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.

QuantitySymbolValue
Endpoint water rel. perm.$k_{rw}^0$0.20
Endpoint oil rel. perm.$k_{ro}^0$0.80
Connate water saturation$S_{wc}$0.20
Residual oil saturation$S_{or}$0.30
Corey exponent (both curves)$n$2
Well spacing (injector-producer)$L$2700 ft
Line-drive cross-sectional area$A$3000 ft²
Porosity$\phi$0.25
Initial water saturation$S_{wi}$0.20 (= $S_{wc}$)
Oil viscosity$\mu_o$3.0 cp
Water viscosity$\mu_w$1.0 cp
Water injection rate$q_i$250 STB/day

Find. (a) $f_w(S_w)$ and the Welge tangent construction; (b) water breakthrough time $t_{BT}$; (c) the 1-D water-saturation profile $S_w(x)$ at 0.20 pore volumes injected.

Approach. Build $f_w(S_w)=1/[1+(k_{ro}\mu_w)/(k_{rw}\mu_o)]$ from the given Corey-type curves, locate the shock (front) saturation $S_{wf}$ by Welge's tangent-line construction from the initial condition $(S_{wc},0)$, then apply the Buckley-Leverett frontal-advance equation $x(S_w,t)=\dfrac{q_i t}{A\phi}\dfrac{df_w}{dS_w}$ for breakthrough and for the saturation profile.

  1. Fractional-flow curve. With $S_e=(S_w-S_{wc})/(1-S_{wc}-S_{or})=(S_w-0.20)/0.50$, the given curves reduce to $k_{rw}=0.20\,S_e^2$ and $k_{ro}=0.80(1-S_e)^2$ (since $S_o-S_{or}=(1-S_{wc}-S_{or})(1-S_e)$). Substituting into $f_w=\left[1+\dfrac{k_{ro}\mu_w}{k_{rw}\mu_o}\right]^{-1}$ gives $$f_w(S_w)=\left[1+\frac{4}{3}\left(\frac{1-S_e}{S_e}\right)^{2}\right]^{-1},\qquad 0.20\le S_w\le 0.70.$$ Evaluating point-by-point (e.g. $S_w=0.40$: $S_e=0.40$, $k_{rw}=0.032$, $k_{ro}=0.288$, $f_w=0.357$; $S_w=0.60$: $S_e=0.80$, $k_{rw}=0.128$, $k_{ro}=0.032$, $f_w=0.923$) traces the S-shaped curve plotted in Fig. 1.
  2. Welge tangent-line construction. Since the reservoir is at connate water ($S_{wi}=S_{wc}=0.20$, no mobile water ahead of the flood), the tangent is drawn from $(S_{wc},f_w)=(0.20,0)$ to the point on the $f_w$ curve that maximizes the secant slope $f_w(S_w)/(S_w-S_{wc})$ — equivalently, the point where the tangent line just touches the curve. A numerical sweep of the curve locates this at $$\boxed{S_{wf}=0.578,\quad f_w(S_{wf})=0.878,\quad \left.\frac{df_w}{dS_w}\right|_{S_{wf}}=2.323}.$$ This is the water-saturation value that propagates as a stable shock front; saturations between $S_{wc}$ and $S_{wf}$ are not physically realized (they would require the curve to be multi-valued in $x$).
  3. Breakthrough time. The dimensionless pore volumes injected at breakthrough is the reciprocal of the tangent slope, $W_{iD,BT}=1/f_w'(S_{wf})=1/2.323=0.4305$ PV. The swept pore volume is $$PV=A\,\phi\,L=3000\times0.25\times2700=2{,}025{,}000\ \text{ft}^3=\frac{2{,}025{,}000}{5.615}=360{,}641\ \text{bbl}.$$ With $q_i=250$ STB/day (taken as 250 res bbl/day, $B_w\approx1$), $$t_{BT}=\frac{PV\cdot W_{iD,BT}}{q_i}=\frac{360{,}641\times0.4305}{250}=\boxed{621\ \text{days}}.$$
  4. Saturation profile at 0.20 PV injected. Since $W_{iD}=0.20\lt W_{iD,BT}=0.4305$, the front has not yet broken through. Each saturation $S_w\in[S_{wf},\,1-S_{or}]$ behind the front travels to $x(S_w)=W_{iD}\,L\,f_w'(S_w)$ (a rearrangement of the frontal-advance equation using $PV/(A\phi)=L$). The front itself sits at $$x_f=W_{iD}\,L\,f_w'(S_{wf})=0.20\times2700\times2.323=\boxed{1254\ \text{ft}}\ (\lt L=2700\text{ ft, confirming pre-breakthrough}).$$ Ahead of the front ($x_f\lt x\le L$) the formation is undisturbed at $S_w=S_{wc}=0.20$; behind it, $S_w$ decreases smoothly from $1-S_{or}=0.70$ at the injector ($x=0$, where $f_w'\to0$) down to $S_{wf}=0.578$ at $x=x_f$, where it drops discontinuously (the shock) to $0.20$. The full profile is plotted in Fig. 2.
0.00.00.20.20.40.40.60.60.80.81.01.0Water Saturation, SwFractional Flow, fwSwf = 0.58
Fig. 1: Water fractional-flow curve $f_w(S_w)$ (blue) with the Welge tangent line from $(S_{wc},0)$ (red dashed), touching the curve at the shock front $S_{wf}=0.578$.
00.005400.2010800.4016200.6021600.8027001.00Distance from Injector, x (ft)Water Saturation, Swshock front
Fig. 2: 1-D water-saturation profile at 0.20 PV injected (t = 288.5 days): smooth spreading wave from $S_w=0.70$ at the injector down to $S_{wf}=0.578$, a shock down to $S_{wc}=0.20$ at $x_f=1254$ ft, then undisturbed formation out to the producer at $L=2700$ ft.
QuantityValue
Front (shock) saturation, $S_{wf}$0.578
$f_w$ at the front0.878
Tangent slope, $f_w'(S_{wf})$2.323
Swept pore volume, $PV$360,641 bbl
Breakthrough pore volumes injected, $W_{iD,BT}$0.4305 PV
Water breakthrough time, $t_{BT}$621 days
Front position at 0.20 PV injected ($t=288.5$ d)1254 ft (pre-breakthrough)
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