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24-Pet-B2 Oil and Gas Evaluation and Economics · Undated paper

Question 4 of 7: Actual and Standard Gas Flow Rates

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

Notes on this paper

National Exams May 2019, 17-Pet-B2, Natural Gas Engineering — 3 hours, open book (non-communicating calculator permitted), 7 questions of equal (10-mark) value. 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.; McCain, The Properties of Petroleum Fluids, 3rd ed.; Mohitpour et al., Pipeline Design and Construction, 3rd ed. (ASME Press); GPSA Engineering Data Book (component critical-property tables); Wichert & Aziz (1972), “Calculate Z's for Sour Gases,” Hydrocarbon Processing; Mandhane, Gregory & Aziz (1974), “A Flow Pattern Map for Gas-Liquid Flow in Horizontal Pipes,” Int. J. Multiphase Flow.

Question 4: Actual and Standard Gas Flow Rates (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. $\rho_b=187.5$ kg/m$^3$ and $V_{m,b}=0.1299$ m$^3$/kmol (Question 3b), $\dot m=33.34$ kg/s (Question 3c), $T_{sc}=60^\circ\text{F}$, $p_{sc}=14.69$ psia.

Find. (a) actual volumetric flow rate at plant conditions, m$^3$/s; (b) standard flow rate in MMSCFD.

Approach. The mass (and molar) flow rate is fixed by continuity regardless of which pressure/temperature it is evaluated at — divide by the plant-condition density from Question 3(b) for part (a), and re-express the same molar flow rate through a field-units standard molar volume for part (b).

  1. (a) Actual volumetric flow rate at plant conditions. $$Q_{actual}=\frac{\dot m}{\rho_b}=\frac{33.34\ \text{kg/s}}{187.5\ \text{kg/m}^3}=\boxed{0.1778\ \text{m}^3/\text{s}}\ \ (=15{,}358\ \text{m}^3/\text{d})$$ Cross-check via the molar route: $Q_{actual}=\dot n\,V_{m,b}=(118{,}230\ \text{kmol/d})(0.1299\ \text{m}^3/\text{kmol})/86{,}400\ \text{s/d}=0.1778\ \text{m}^3/\text{s}$ — matches.
  2. (b) Standard flow rate at 60°F/14.69 psia. Convert the same molar flow rate to field units and apply the ideal-gas standard molar volume ($Z_{sc}\approx1$): $$\dot n=118{,}230\ \text{kmol/d}\times2.2046=260{,}653\ \text{lbmol/d}$$ $$V_{m,sc}=\frac{RT_{sc}}{p_{sc}}=\frac{10.732(519.67)}{14.69}=379.7\ \text{ft}^3/\text{lbmol}$$ $$Q_{sc}=\dot n\,V_{m,sc}=260{,}653(379.7)=9.90\times10^{7}\ \text{scf/d}=\boxed{98.96\ \text{MMSCFD}}$$
QuantityResult
(a) Actual volumetric flow rate, $Q_{actual}$0.1778 m$^3$/s (15,358 m$^3$/d)
(b) Standard flow rate, $Q_{sc}$98.96 MMSCFD