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Led by Senior Rotating Equipment Engineer Simulacrum
Pump operation and maintenance from pump types and performance curves through BEP, NPSH, cavitation, startup and control systems, preventive and predictive maintenance, mechanical seals, alignment, lubrication, troubleshooting, and energy efficiency.
Led by Senior Rotating Equipment Engineer Simulacrum
The question
Every pump converts mechanical energy into fluid energy — but the two fundamental categories differ in how. This module covers centrifugal pump operating principles (impeller, volute, velocity-to-pressure conversion), five centrifugal types (single-stage through submersible), positive displacement principles (fixed volume per revolution, flow independent of pressure), four PD types (piston, screw, gear, lobe), the seven pump components and their functions (impeller, casing, shaft, bearings, mechanical seal, coupling, baseplate), and API 682 seal flush plans.
Outcome
The student can describe both pump categories, name their subtypes, describe the seven components, explain three seal flush plans, and explain when each pump category is preferred. (Pump types, components, and principles)
Sub-units
Led by Senior Rotating Equipment Engineer Simulacrum
The question
The pump performance curve is the most important document in the pump engineer's toolkit — it defines what the pump delivers at every operating point. This module covers reading the H-Q, efficiency, power, and NPSHr curves, constructing the system curve and finding the operating point, the BEP and the acceptable 70–120% operating range, the consequences of operating off-BEP (suction and discharge recirculation), NPSH calculation and the cavitation mechanism, pump selection from duty and fluid properties, and suction piping installation requirements.
Outcome
The student can read a pump curve, find the operating point, calculate NPSHa, compare it to NPSHr, apply the affinity laws for speed changes, and describe the suction piping requirements. (Pump performance, selection, and installation)
Sub-units
Led by Senior Rotating Equipment Engineer Simulacrum
The question
Most pump failures are caused not by defective equipment but by incorrect operation — starting unprimed, running at dead-head, or tripping without depressurisation. This module covers centrifugal pump startup procedure (priming, rotation check, starting against closed discharge), PD pump startup (discharge must be open — overpressure risk), the five parameters monitored during normal operation, three pump control methods (throttle valve, VFD with affinity law savings, minimum-flow recirculation for low-flow protection), and shutdown, standby, and automatic switchover procedures.
Outcome
The student can describe the startup procedure for both pump types, explain the five monitored parameters, describe the three control methods with VFD energy savings, and explain the automatic switchover logic. (Pump operation and control)
Sub-units
Led by Senior Rotating Equipment Engineer Simulacrum
The question
Pump maintenance consumes more budget than any other equipment category — because there are so many pumps and they have wearing components. This module covers the preventive maintenance schedule (daily through overhaul, including wear ring tolerances and shaft runout), four predictive techniques (vibration spectrum analysis for fault diagnosis, oil analysis, thermography, ultrasonic), mechanical seal inspection and replacement (face damage types, O-ring criteria, installation precision), shaft alignment by dial indicator and laser, and three lubrication methods (oil with constant-level oiler, grease with over-greasing risk, oil mist systems).
Outcome
The student can describe the preventive schedule, interpret a vibration spectrum to diagnose four faults, describe the seal inspection and replacement procedure, describe both alignment methods, and describe three lubrication methods. (Pump maintenance)
Sub-units
Led by Senior HSE Engineer Simulacrum
The question
When a pump fails, the troubleshooter checks the suction first, then the pump, then the discharge — because most problems originate at the suction. This module develops the diagnostic methodology for six pump problems (no flow, low flow, high vibration, excessive noise, seal leakage, high bearing temperature), energy efficiency practices (VFD vs. throttle valve savings calculated from the affinity laws, impeller trimming for oversized pumps, system piping optimisation), and five safety hazards around pumps (entanglement, high pressure, high temperature, chemical exposure, LOTO) with the control for each.
Outcome
The student can diagnose six pump problems from symptoms, calculate the VFD energy saving, describe three system optimisation measures, and describe five safety hazards with their controls. (Troubleshooting, energy efficiency, and safety)
Sub-units