24-Pet-A3 Fundamental Reservoir Engineering · May 2016
Question 3 of 7: Bottom-Hole Pressure Near a Sealing Fault (Method of Images)
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
98-Pet-A3 — Fundamental Reservoir Engineering · National Exams, May 2016 · 3 hours, closed book, non-communicating calculator only · five (5) questions constitute a complete exam paper (the first five as they appear in the answer book are marked), all questions equal value, all parts of a multipart question equal weight.
Reference texts: Ahmed, T., Reservoir Engineering Handbook, 5th ed. (Darcy's law, transient well testing and image wells, p/Z and oil material balance, capillary pressure/relative permeability); Craft, B.C. & Hawkins, M.F., Applied Petroleum Reservoir Engineering, 3rd ed. (steady-state radial flow, reservoir drive mechanisms); Lyons, W.C. (ed.), Standard Handbook of Petroleum and Natural Gas Engineering, 3rd ed.; McCain, W.D., The Properties of Petroleum Fluids, 3rd ed. (capillary pressure and relative permeability laboratory data).
Question 3: Bottom-Hole Pressure Near a Sealing Fault (Method of Images) (20 marks)
Find. The bottom-hole (flowing wellbore) pressure of the well after 1 day of production at 250 STBD, accounting for the nearby sealing fault.
Fig. 1 — A sealing fault is modelled by the method of images: an imaginary well of the same rate is placed a mirror distance $L$ beyond the fault, so its added pressure drop reproduces the fault's no-flow condition.
Approach. A single sealing (no-flow) fault is modelled by superposition: place an image well of the same rate at twice the well-to-fault distance ($2L=500$ ft) and add its pressure-drop contribution to the real well's own (infinite-acting) contribution. Compute $t_D$ at $r=r_w$ (real well) and at $r=2L$ (image well); since the exam's own formula sheet states the log approximation $p_D=0.5(\ln t_D+0.809)$ is valid "only if $t_D>100$", check each $t_D$ and use the exact line-source form $p_D=0.5[-Ei(-1/4t_D)]$ wherever it is not.
Diffusivity constant. With $k=100\ \text{mD}=0.1$ Darcy (the formula sheet's transient equations use $k$ in Darcy, consistent with its steady-flow equation), $\eta=\dfrac{6.33k}{\phi\mu c_t}=\dfrac{6.33(0.1)}{(0.20)(2)(6\times10^{-6})}=263{,}750\ \text{ft}^2/\text{day}$.
Real well contribution. At $r=r_w=0.33$ ft, $t=1$ day: $t_D=\eta t/r_w^2=263{,}750/0.33^2=2.42\times10^6$. Since $t_D>100$, use the log form: $\boxed{p_D=0.5(\ln t_D+0.809)=0.5(14.70+0.809)=7.755}$.
Image-well contribution. At $r=2L=500$ ft: $t_D=\eta t/(500)^2=263{,}750/250{,}000=1.055$. Since $t_D<100$, the log form is invalid; use the exact line-source form: $\boxed{p_D=0.5[-Ei(-1/(4\times1.055))]=0.5[-Ei(-0.2370)]=0.543}$.
Bottom-hole pressure. $\dfrac{0.141\,q\mu B_o}{kh}=\dfrac{0.141(250)(2)(1.25)}{(0.1)(100)}=8.81$ psi. Superposing both wells (no skin given), $\Delta p=8.81\,(p_{D,\text{real}}+p_{D,\text{image}})=8.81(7.755+0.543)=8.81(8.298)=73.1$ psi. $\boxed{p_{wf}=p_i-\Delta p=3000-73.1=2926.9\ \text{psia}}$.