24-Pet-A2 Petroleum Reservoir Fluids · Undated paper
Question 5 of 6: Reservoir Oil & Gas Density and Flow Rates
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
EGBC National Exam — Petroleum Engineering, 17-Pet-A2 Petroleum Reservoir Fluids, National Examinations May 2019. 3 hours duration, closed book, formula sheet supplied, personal scientific calculator permitted. SIX questions are printed on the paper; per the exam's own instructions, any FIVE constitute a complete answer paper. Every question is solved in full below (all six, not just the five a candidate would normally submit) so this set also serves as complete study material.
Reference texts: McCain, W.D., The Properties of Petroleum Fluids, 3rd ed. (PennWell); Ahmed, T., Reservoir Engineering Handbook, 5th ed.; Standing, M.B., Volumetric and Phase Behavior of Oil Field Hydrocarbon Systems; Craft, B.C. & Hawkins, M.F., Applied Petroleum Reservoir Engineering, 3rd ed.
Check: two graphical-correlation questions (4B's Carr et al. gas-viscosity chart, and 6a's Standing-Katz z-factor chart) are answered using the standard published Lee-Gonzalez-Eakin (1966) gas-viscosity correlation and the Dranchuk & Abou-Kassem (1975) z-factor equation of state respectively – both are the accepted numerical proxies for reading these two charts precisely, and are flagged again at each point of use.
Question 5: Reservoir Oil & Gas Density and Flow Rates (20 marks)
Find. (a) ρo,res, ρg,res; (b) qo,res, qg,res; (c) phase state and saturation.
Approach. Build a mass balance per stock-tank barrel of oil (oil mass + dissolved-gas mass, divided by the reservoir volume that mass occupies) for ρo,res; use ρg,sc/Bg (converted to consistent volume units) for ρg,res; convert surface rates to reservoir rates using Bo and Bg; then compare the produced GOR against Rs to test for free gas.
(a) Reservoir densities
Gas density at standard conditions. $\rho_{g,sc}=\gamma_g\times\rho_{air,sc}=0.67\times0.076=0.0509\text{ lb/ft}^3$
Mass balance per STB of oil. 1 STB = 5.615 ft³, so the oil mass is $53\times5.615=297.6$ lb; the dissolved-gas mass carried with it is $R_s\times\rho_{g,sc}=347\times0.0509=17.67$ lb. Total mass $=297.6+17.67=315.3$ lb.
Reservoir oil density. That same STB of oil occupies $B_o\times5.615=1.19\times5.615=6.682\text{ ft}^3$ at reservoir conditions, so
$$\rho_{o,res}=\frac{315.3}{6.682}=\boxed{47.2\text{ lb/ft}^3}$$
Reservoir gas density. 1 SCF of gas (mass $\rho_{g,sc}=0.0509$ lb) occupies $B_g\times5.615=0.0012\times5.615=0.00674\text{ ft}^3$ at reservoir conditions:
$$\rho_{g,res}=\frac{0.0509}{0.00674}=\boxed{7.56\text{ lb/ft}^3}$$
(b) Reservoir flow rates
Oil rate in the reservoir converts directly through Bo:
$$q_{o,res}=q_{o,sc}\times B_o=2000\times1.19=\boxed{2380\text{ rb/day}}$$
Split the produced gas into solution gas and free gas. Solution gas travelling with the oil $=q_{o,sc}\times R_s=2000\times347=694{,}000$ SCF/day. The remainder is free gas: $2{,}000{,}000-694{,}000=1{,}306{,}000$ SCF/day.
Free-gas rate in the reservoir converts through Bg:
$$q_{g,res}=1{,}306{,}000\times0.0012=\boxed{1567\text{ rb/day}}$$
(c) Phase state and saturation
The produced (total) GOR is $q_{g,sc}/q_{o,sc}=2{,}000{,}000/2000=1000$ SCF/STB, which is greater than the solution GOR at current reservoir pressure, Rs = 347 SCF/STB. Because more gas is being produced than the oil can hold in solution at this pressure, free gas must already exist and be flowing in the reservoir near the wellbore. The reservoir is therefore currently in a two-phase (oil + gas) state, and because free gas is present at the current pressure, the remaining oil is at its bubble point – a saturated reservoir.
Question 5 – results
Quantity
Value
Reservoir oil density
47.2 lb/ft³
Reservoir gas density
7.56 lb/ft³
Reservoir oil flow rate
2380 rb/day
Reservoir free-gas flow rate
1567 rb/day
Phase state
Two-phase, saturated (produced GOR 1000 > Rs 347 SCF/STB)