PRODUCTION ENGINEERING / SIMULATION LAB

LiftLab

Gas lift · ESP · Sucker-rod pump
Educational steady-state models
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EXPLORE THE OPERATING WINDOW

Three ways to lift a well.

Change the well. Tune the equipment. Compare the response.

Each curve changes only the selected operating control; all other inputs remain fixed. Rates are liquid volume at model conditions, with formation volume factor assumed 1.

Model equations & boundaries

Inflow: Pwf = Pr − Q / PI. Outflow: Pwh + ρgD / 10⁶ + kQ² (MPa). Constant density, linear PI, vertical well and steady flow are assumed.

Gas lift: illustrative gas fraction α = 0.65I / (I + 10,000); effective density = ρ(1 − α); added friction = 2 × 10⁻⁹I² MPa. I is standard m³/d. This deliberately simplified response is not a validated multiphase or gas-expansion correlation.

ESP: H = N × 12 × [(f/50)² − (Q/400)²] m within the reference curve. N is stage count. Generic 50 Hz reference curve, not a manufacturer's pump. Power = ρgQH / η with Q in m³/s and η = 0.65. Operating rate solves inflow versus outflow minus pump boost.

Sucker-rod: Q = πd²S × SPM × 1440 × fillage / 4, capped by reservoir supply at an assumed 1 MPa minimum intake pressure. Downhole stroke is specified directly. Power uses required hydraulic boost / 0.65. Fluid load excludes rod weight, inertia, friction and stress.

Educational comparison only. No gas-lift valve design, compressor power, ESP gas handling, viscosity corrections, motor limits, rod dynamics or field calibration. A larger predicted rate does not establish the best lift method. Pump setting depth equals reservoir depth. No cost ranking is implied.

Suggested experiments & references
  1. Sweep gas injection and observe the competition between density reduction and friction.
  2. Change ESP frequency or stage count and inspect the production response.
  3. Reduce reservoir pressure and increase rod-pump speed to observe the supply cap.

SLB: Artificial lift · KSB: Pump affinity laws

These references support the operating principles; all numerical equipment curves and gas-lift coefficients here are illustrative assumptions.