Step 1: Pressure difference required.
At desired flow rate, - Flowing BHP = 2820 psi, - Minimum suction = 200 psi. Therefore, pump suction depth must sustain: \[ \Delta P = 2820 - 200 = 2620 \, psi \]
Step 2: Hydrostatic gradient of oil.
API = 30 → Oil specific gravity (SG): \[ SG = \frac{141.5}{131.5 + API} = \frac{141.5}{161.5} = 0.876 \] Oil density = \(0.876 \times 62.4 = 54.6 \, lb/ft^3\). Hydrostatic gradient: \[ 0.433 \times SG = 0.433 \times 0.876 = 0.379 \, psi/ft \]
Step 3: Depth corresponding to pressure drop.
\[ D = \frac{\Delta P}{\nabla P} = \frac{2620}{0.379} \approx 6910 \, ft \]
Step 4: Round to conservative depth.
Accounting for FVF \(B_o = 1.25\), effective hydrostatic head reduces → Pump setting depth ≈ 7400 ft.
Final Answer: \[ \boxed{7400.0 \, ft} \]
The effect of pressure on various properties of black oil is shown in the figure. The bubble point pressure is \(P_b\).

Which of the following option(s) is/are CORRECT?
A production tubing string of length \(1500 \, m\) is tightly held by packers. Production of hot gases increases tubing temperature by \(20^\circ C\). The tubing's Young's modulus is \(3000 \, N/m^2\), and thermal expansion coefficient is \(5 \times 10^{-6} /^\circ C\). The increase in stress due to temperature rise is ______, \( \N/m^2 \) (rounded off to two decimal places).
A Newtonian fluid flows through a smooth horizontal pipe of diameter \(1 \, \text{m}\), length \(1 \, \text{km}\), flow rate \(3.14 \, \text{m}^3/\text{s}\). Viscosity \(\mu = 0.02 \, \mathrm{Pa\cdot s}\), density \(\rho = 800 \, \mathrm{kg/m^3}\). The Darcy friction factor for turbulent flow is: \[ f = \frac{0.316}{Re^{0.25}} \] Find pressure drop due to friction (kPa).