AGR-WATE71-04 · Lesson 5 · 13 clock hours · lab
Pump Operation, Startup, and Shutdown
Objective. Students start, operate, and shut down a centrifugal pump following a written standard operating procedure and record performance data including flow, suction pressure, discharge pressure, amperage, and vibration.
⚠ Pending professional review
This lesson, its worked examples and its practice questions has not yet been verified by a licensed professional in the field or by a certification or approval body. It is a study draft and may contain errors. Do not use it as instructions for work on a job site or on live equipment. Always follow your instructor, your supervising professional, and current official references and regulations.
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Pump Operation, Startup, and Shutdown
Why This Skill Matters
Centrifugal pumps move treated water through distribution systems and raw or treated wastewater through collection and treatment systems. An operator who starts or stops a pump incorrectly can cause water hammer, seal failure, motor burnout, or a loss of system pressure that threatens public health. Licensing exams for Class I and Class II water and wastewater operators test pump knowledge directly, and every licensed facility requires operators to follow a written Standard Operating Procedure (SOP) for pump work.
How a Centrifugal Pump Works
A centrifugal pump uses a rotating impeller to add velocity to liquid. That velocity converts to pressure as the liquid slows in the volute casing. The pump draws liquid in through the suction port and discharges it under pressure through the discharge port. Key performance points are:
- Flow rate – how many gallons per minute (gpm) the pump delivers
- Total Dynamic Head (TDH) – the total pressure the pump works against, measured in feet of head or pounds per square inch (psi)
- Efficiency – the ratio of hydraulic power output to motor power input
- Best Efficiency Point (BEP) – the design flow at which the pump operates most efficiently and with the least mechanical stress
Operating far from the BEP increases vibration, heat, and wear.
Safety First
Before touching any pump or motor, identify all energy sources and apply your facility's lockout/tagout (LOTO) program whenever you are performing maintenance. For this lab, the instructor controls energy isolation. During operation:
- Wear safety glasses at all times in the pump room.
- Wear hearing protection when noise levels are elevated; rotating equipment can exceed safe exposure limits.
- Keep hands and clothing away from rotating shafts and coupling guards. Never remove a coupling guard while the pump is running.
- Be aware of slipping hazards from water on the floor.
- Know the location of the emergency stop before startup.
Pre-Operation Walkthrough
A written pre-start checklist prevents the most common startup mistakes. Complete every item before requesting instructor authorization:
1. Packing or mechanical seal – Inspect for leaks or damage. A small controlled drip from packing glands is normal; mechanical seals should show no visible leakage.
2. Lubrication – Check oil level or grease fittings per the manufacturer's specification.
3. Suction valve – Confirm it is fully open. Starting with a closed suction valve causes cavitation or no flow.
4. Discharge valve position – For most centrifugal pumps, start with the discharge valve partially closed to reduce startup load on the motor, then open slowly after startup. Follow your SOP; some systems differ.
5. Coupling guard – Verify the guard is in place and secured.
6. Prime – Confirm the pump casing and suction line are filled with liquid. A centrifugal pump cannot self-prime in most configurations; running dry damages the seal and impeller rapidly.
Supervised Startup Sequence
1. Confirm pre-start checklist is signed off.
2. Start the motor. Listen for abnormal noise immediately.
3. Slowly open the discharge valve while watching the discharge pressure gauge rise steadily.
4. Check suction pressure gauge. Suction pressure should remain positive (above atmospheric) or within the expected range for your system.
5. Check for unusual vibration by touch or with a vibration tester.
6. Measure motor amperage with a clamp meter on one phase lead. Compare to the nameplate full-load amperage (FLA).
7. Record all readings on your operations log at 0 minutes (just after valve is open), 5 minutes, and 15 minutes.
Data fields to record each interval: time, suction pressure (psi), discharge pressure (psi), flow rate (gpm), motor amperage (A), and vibration level or observation.
Reading the Pump Curve
The pump curve is a graph published by the manufacturer. The x-axis shows flow (gpm) and the y-axis shows head (feet or psi). As flow increases, head decreases along the curve. A separate efficiency curve peaks at the BEP. When you compare your recorded data to the pump curve:
- Plot your measured flow and calculated head on the curve.
- If your point falls far to the left (low flow, high head), the discharge valve may be too closed or there is a blockage.
- If your point falls far to the right (high flow, low head), the system resistance is lower than expected, and the motor may be overloaded.
Controlled Shutdown Sequence
1. Slowly close the discharge valve before stopping the motor to prevent water hammer in most centrifugal pump installations.
2. Stop the motor.
3. Close the suction isolation valve if required by the SOP.
4. Record final readings.
5. Inspect the pump for any leaks or unusual conditions before leaving the area.
Post-Run Log Review
After shutdown, compare each recorded parameter to the nameplate ratings and pump curve. For any reading outside the acceptable range, write a brief corrective note explaining the likely cause and recommended action. This habit is required practice for licensed operators and reflects what exam questions call "troubleshooting" or "operational analysis."
Connecting to the License Exam
State Class I and Class II operator exams include questions on pump operation, reading gauges, interpreting pump curves, identifying cavitation, and calculating flow and pressure. Accurate log-keeping also demonstrates the professional standard regulators expect from licensed operators.
Key terms9
Centrifugal pumpA pump that uses a rotating impeller to impart velocity to liquid, converting that velocity to pressure in the volute casing.
Total Dynamic Head (TDH)The total equivalent height of liquid that a pump must overcome, accounting for static lift, friction losses, and pressure differences; commonly expressed in feet of head or psi.
Best Efficiency Point (BEP)The flow rate at which a centrifugal pump operates at its highest hydraulic efficiency and lowest mechanical stress, as shown on the pump curve.
CavitationA condition in which the liquid pressure at the pump suction drops below the vapor pressure of the liquid, forming and collapsing vapor bubbles that cause noise, vibration, and impeller damage.
Pump curveA manufacturer-supplied graph showing the relationship between flow rate and head (and often efficiency and power) for a specific pump model.
Full-Load Amperage (FLA)The motor current draw shown on the nameplate when the motor is delivering its rated horsepower; used as a reference to detect overloading or underloading.
Water hammerA pressure surge or wave created when liquid in motion is forced to stop or change direction suddenly, often caused by rapid valve closure or improper pump shutdown.
Lockout/Tagout (LOTO)A safety procedure that isolates all energy sources to equipment and applies physical locks and warning tags before maintenance is performed, preventing accidental startup.
Standard Operating Procedure (SOP)A written, step-by-step instruction document that operators must follow to perform a task consistently, safely, and in compliance with regulatory requirements.
Worked examples4
1. Convert suction and discharge gauge readings to Total Dynamic Head (TDH). The suction gauge reads 5 psi (positive, meaning above atmospheric) and the discharge gauge reads 65 psi. What is the differential pressure across the pump in psi, and what is that in feet of head for fresh water?
- Step 1 – Find differential pressure: Discharge pressure − Suction pressure = 65 psi − 5 psi = 60 psi.
- Step 2 – Convert psi to feet of head using the conversion factor for fresh water: 1 psi = 2.31 feet of head.
- Step 3 – Multiply: 60 psi × 2.31 ft/psi = 138.6 feet of head.
Answer: The differential pressure is 60 psi, which equals approximately 138.6 feet of TDH for fresh water.
2. A pump's nameplate shows a Full-Load Amperage (FLA) of 18 A. Your clamp meter reads 21 A during the 15-minute log entry. By what percentage does the measured amperage exceed the nameplate FLA, and what does this suggest?
- Step 1 – Find the excess amperage: 21 A − 18 A = 3 A above nameplate.
- Step 2 – Calculate the percentage over FLA: (3 A ÷ 18 A) × 100 = 16.7% over FLA.
- Step 3 – Interpret: The motor is drawing about 17% more current than its rated FLA, indicating the pump may be operating to the far right of its curve (too much flow), the motor may be undersized, or there may be a mechanical issue. This reading should be flagged and investigated.
Answer: The amperage is 16.7% above nameplate FLA, which is outside normal range and requires a corrective note in the operations log.
3. Your operations log shows a flow of 120 gpm and a TDH of 80 feet. The pump curve shows that at 120 gpm the pump should develop 95 feet of TDH. What is the head deficit in feet, and what could explain it?
- Step 1 – Find the head deficit: Expected head − Measured head = 95 ft − 80 ft = 15 ft deficit.
- Step 2 – Express as a percentage: (15 ÷ 95) × 100 ≈ 15.8% below the curve.
- Step 3 – Interpret: A measured head lower than the curve predicts at the same flow suggests the pump is worn (impeller wear reduces head), air entrainment in the casing, or the pump is operating in a cavitating condition. Flag this reading and note the likely causes.
Answer: There is a 15-foot (approximately 15.8%) head deficit compared to the pump curve at 120 gpm, which should be investigated for impeller wear, air entrainment, or cavitation.
4. A pump runs for 2 hours and moves water through a 6-inch main. The flow meter averages 350 gpm. How many gallons does the pump deliver in that period?
- Step 1 – Convert run time to minutes: 2 hours × 60 min/hour = 120 minutes.
- Step 2 – Multiply average flow rate by total minutes: 350 gpm × 120 min = 42,000 gallons.
Answer: The pump delivers 42,000 gallons over the 2-hour run period.
The math in this lesson1
Learners convert 60 psi differential pressure to 138.6 ft of head with 2.31 ft/psi.
N-Q.1
In class: Pre-operation walkthrough: students complete a written pre-start checklist (packing/seal condition, lubrication, suction valve open, discharge valve position, coupling guard in place) on the lab pump trainer before the instructor authorizes startup. · Supervised startup: students start the pump, slowly open the discharge valve, observe pressure gauges, check for unusual noise or vibration, measure motor amperage with a clamp meter, and record all data on an operations log at 0, 5, and 15 minutes. · Controlled shutdown and log review: students shut down the pump following the SOP sequence, close isolation valves, and then compare their recorded performance data to the pump curve and nameplate ratings—flagging any readings outside normal range and writing a brief corrective note.
Materials: Lab pump trainer (centrifugal pump with suction and discharge gauges, flow meter, clamp meter), vibration tester or handheld probe, operations log forms, SOP template, hearing protection, safety glasses
Check: Student operations log must contain all required data fields completed accurately and the post-run analysis must correctly identify whether each parameter is within the acceptable range; pass mark is 75% of data fields correct with no safety-critical steps skipped.
Practice check8
Answer each question, then check it. Nothing is recorded; this is your own practice.
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