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24-Pet-A6 Well Logging and Formation Evaluation · May 2017

Question 2 of 8

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

Notes on this paper

Paper format: National Exams, May 2017 – 98-Pet-A6, Reservoir Mechanics (3 hours, open book, non-communicating calculator permitted). The exam consists of EIGHT questions; candidates respond to 100 marks of their choice out of 120. All eight questions are answered in full below.

Reference texts: Craft, B.C. and Hawkins, M. (rev. Terry & Rogers), Applied Petroleum Reservoir Engineering, 3rd ed.; Ahmed, T., Reservoir Engineering Handbook, 5th ed.; Lyons, W.C. (ed.), Standard Handbook of Petroleum and Natural Gas Engineering, 3rd ed.

If doubt exists..." "2. This is an OPEN BOOK EXAM..." "3. The exam consists of EIGHT (8) questions..." "4. Clarity and organization...") immediately above Question 1. every real "Question N" heading on this paper parses cleanly (checked by direct read of the source), so it does not affect the answers below.

Question 2 (10 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. Steady, incompressible linear (Darcy) flow updip through a tilted bed, with the outlet cross-section as the representative flow area.

Inletp1 = 2,100 psiOutletp2 = ?L = 2,500 ftW = 500 ft, h = 30 ftθ = 7°k = 60 md, φ = 20%, μ = 2 cp, ρ = 44 lb/ft3, Q = 5 bbl/day
Fig. Q2 – tilted linear porous medium, flow from the lower inlet to the higher outlet face.

Find. The outlet pressure $p_2$.

Approach. Apply Darcy's law for tilted linear flow, which combines a viscous pressure-drop term with a hydrostatic (gravity) term because the flow is updip.

  1. Fluid specific gravity and flow area. $\gamma=\rho/62.4=44/62.4=0.7051$ (relative to water). Using the given outlet face as the (uniform) flow area, $A=W\times h=500\times30=15{,}000\text{ ft}^2$.
  2. Darcy's law for tilted linear flow. $$q=\frac{1.127\times10^{-3}\,kA}{\mu L}\Big[(p_1-p_2)-0.433\gamma L\sin\theta\Big]$$ Rearranging for $p_2$: $$p_2=p_1-\underbrace{\frac{q\mu L}{1.127\times10^{-3}kA}}_{\text{viscous drop}}-\underbrace{0.433\gamma L\sin\theta}_{\text{elevation (gravity) term}}$$
  3. Viscous pressure drop. $$\Delta p_{visc}=\frac{(5)(2)(2{,}500)}{1.127\times10^{-3}(60)(15{,}000)}\approx 24.6\text{ psi}$$
  4. Elevation (gravity) term. $$\Delta p_{grav}=0.433(0.7051)(2{,}500)\sin(7^\circ)\approx 93.0\text{ psi}$$ This is the larger of the two terms – the well must overcome most of the pressure difference simply to lift the oil up the $7^\circ$ dip, since the flow rate (5 bbl/day through a 15,000 ft² face) is very slow.
  5. Outlet pressure. $$p_2=2{,}100-24.6-93.0$$ $$\boxed{p_2\approx 1{,}982.3\text{ psi}}$$
Question 2 – final results
QuantityValue
Specific gravity, $\gamma$0.705
Viscous pressure drop24.6 psi
Elevation (gravity) term93.0 psi
Outlet pressure, $p_2$1,982.3 psi