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24-Pet-B2 Oil and Gas Evaluation and Economics · May 2015

Question 5 of 7: Well Pressure via Real Gas Pseudopressure — Two-Rate Superposition

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

Notes on this paper

National Exams May 2015, 98-Pet-B2, Natural Gas Engineering — 3 hours, closed book (non-communicating calculator permitted), 7 questions of 20 marks each. NOTES item 5 states only the first five questions in the answer book are marked; all 7 are solved.

Reference texts: Katz et al., Handbook of Natural Gas Engineering; Lee & Wattenbarger, Gas Reservoir Engineering (SPE Textbook Series Vol. 5); Ahmed, Reservoir Engineering Handbook, 5th ed.; Mohitpour et al., Pipeline Design and Construction, 3rd ed. (ASME Press); McCain, The Properties of Petroleum Fluids, 3rd ed.

Question 5: Well Pressure via Real Gas Pseudopressure — Two-Rate Superposition (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. $p_i=2000$ psia; $T=580^{\circ}$R; $h=39$ ft; $\phi=0.15$; $k=20$ mD; $r_w=0.4$ ft; $c_t=0.00053$ psi$^{-1}$; $\mu=0.0158$ cp; $q_1=7$ MMSCFD $=7000$ MSCFD for $0\le t<36$ hr, then $q_2=21$ MMSCFD $=21{,}000$ MSCFD for $36\le t\le108$ hr. The $\psi(p)$ function is given graphically (points read at $p=0,500,1000,\ldots,2500$ psia: $\psi=0,\,0.25,\,1.05,\,2.1,\,3.4,\,5.0\ (\times10^8)$ psia$^2$/cp).

Find. $p_{wf}$ after 108 hours of two-rate production.

Approach. The rate changed partway through, so the constant-rate pseudopressure-drop equation cannot be applied directly — use superposition in time: treat the history as two rate increments ($\Delta q_1=q_1$ at $t=0$, and $\Delta q_2=q_2-q_1$ at $t=36$ hr), and sum each increment’s own pseudopressure-drop contribution evaluated at its own elapsed time since it began.

  1. Diffusivity/time-group. $\eta=6.33k/(\phi\mu c_t)=6.33(0.020)/(0.15\times0.0158\times0.00053)$: $\eta=1.008\times10^5\ \text{ft}^2/\text{day}$ ($k=20$ mD $=0.020$ Darcy, per the formula sheet’s stated units).
  2. Dimensionless times for each rate increment. $\Delta q_1$ has been flowing for the full $t=108$ hr $=4.5$ day: $t_{D,1}=\eta t/r_w^2=1.008\times10^5(4.5)/0.4^2=2.835\times10^6$. $\Delta q_2$ has been flowing for $108-36=72$ hr $=3.0$ day: $t_{D,2}=1.008\times10^5(3.0)/0.4^2=1.890\times10^6$. Both exceed 100, so the log-approximation $p_D=0.5(\ln t_D+0.809)$ applies to each: $p_{D,1}=0.5(\ln(2.835\times10^6)+0.809)=7.833$; $p_{D,2}=0.5(\ln(1.890\times10^6)+0.809)=7.630$.
  3. Superposition sum for the total pseudopressure drop. $\psi_i-\psi_{wf}=\dfrac{1.422T}{kh}\left[\Delta q_1\,p_{D,1}+\Delta q_2\,p_{D,2}\right]=\dfrac{1.422(580)}{20(39)}\left[7000(7.833)+14{,}000(7.630)\right]$: $\boxed{\Delta\psi=1.709\times10^5\ \text{psia}^2/\text{cp}}$.
  4. Convert to pressure via the $\psi(p)$ curve. $\psi_i=\psi(p_i=2000)=3.400\times10^8$ psia$^2$/cp (from the given graph). $\psi_{wf}=\psi_i-\Delta\psi=3.400\times10^8-1.709\times10^5=3.39829\times10^8$ psia$^2$/cp. Reading the inverse of the $\psi(p)$ curve at this value: $\boxed{p_{wf}=1999.3\ \text{psia}}$.

[Figure not reproduced: Fig. 2 — Real gas pseudopressure $\psi$ vs. pressure $p$ (source chart), with $\psi_i$ at the initial reservoir pressure and $\psi_{wf}$ after 108 hr of two-rate production marked — the two points are nearly coincident because the total pseudopressure drop is small relative to $\psi_i$. See the official exam paper.]

QuantityValue
Diffusivity group, $\eta$$1.008\times10^5$ ft$^2$/day
$t_{D,1}$ (full 108 hr), $t_{D,2}$ (last 72 hr)$2.835\times10^6$, $1.890\times10^6$
Total pseudopressure drop, $\Delta\psi$$1.709\times10^5$ psia$^2$/cp
$\psi_{wf}$ at $t=108$ hr$3.398\times10^8$ psia$^2$/cp
Well pressure, $p_{wf}$ at $t=108$ hr1999.3 psia
the $\psi(p)$ curve depends only on gas composition and $T$ (not on $k,h,\phi,r_w,c_t,\mu$), both of which match, and the axis ranges of the two charts are identical.