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).
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.
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.
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 $x$).
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, $B_w\approx1$), $$t_{BT}=\frac{PV\cdot W_{iD,BT}}{q_i}=\frac{360{,}641\times0.4305}{250}=\boxed{621\ \text{days}}.$$
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.
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 $S_{wf}=0.578$.
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.