The impeller of a centrifugal pump rotates at high angular velocity. Consequently, the vanes of the impeller hit the fluid, generating turbulent vortex shedding, wake interactions with the cutwater (volute tongue), and blade-pass frequency pressure pulsations. This dynamic energy is transmitted as mechanical vibration through the shaft, bearings, pump casing, and attached piping. The surrounding air and resonant pipe walls then radiate these pulsations as acoustic sound pressure waves, creating an industrial noise hazard.
⚠️ ENGINEERING NOTICE & EDUCATIONAL DISCLAIMER: This interactive acoustic calculator is provided exclusively for preliminary estimation and educational purposes. It utilizes empirical correlations developed by pump manufacturers (Sihi) for sound power under normal operating conditions. It does not account for resonance, motor cooling fans, piping acoustic radiation, or severe cavitation. For detailed plant acoustic safety and compliance with OSHA / ISO standards, certified manufacturer test bay acoustic data must be obtained.
🔊 Centrifugal Pump Noise Level Calculator
Estimate Sound Power Level \(L_{wA}\) and Sound Pressure Level \(L_p\) at distance according to pump type and absorbed power.
Unit System:
Acoustic Calculation Results
A-Weighted Sound Power Level (\(L_{wA}\)):-- dB(A)
Sound Pressure Level at Distance (\(L_p\)):-- dB(A)
OSHA / ISO 8-Hour Daily Limit (85 dB(A)):--
Correlation Applicability Status:--
2. Noise of a centrifugal pump : step by step calculation
How to estimate what will be the noise emitted by a pump ?
2.1 STEP 1 : Define the type of pump
Different hydraulic designs of centrifugal pumps emit distinct acoustic spectra and total sound power levels. The primary industrial categories defined in acoustic empirical standards include:
Side channel pump: Self-priming peripheral impellers with high differential pressure across small chambers.
Single stage volute or ring section pumps with multi impellers: Standard industrial process pumps (ISO 2858 / API 610 single-stage or ring section pumps).
Multi-stage ring section pump: High pressure boiler feed or reverse osmosis booster pumps with multiple stage diffuser casings.
2.2 STEP 2 : Calculate the absorbed power
The absorbed mechanical power \(P\) delivered by the electric motor to the pump shaft is calculated from the mass flow rate, total developed head, fluid density, and overall pump hydraulic efficiency:
2.3 STEP 3 : Calculate the noise emitted (Sound Power Level \(L_{wA}\))
According to extensive experimental acoustic surveys compiled by pump manufacturer Sihi [Sihi], the total A-weighted sound power level emitted by the pump casing under nominal hydraulic duty is expressed as a logarithmic function of absorbed power:
\(L_{wA}\) = A-weighted sound power level in \(\text{dB(A)}\) (referenced to \(10^{-12}\text{ W}\))
\(P\) = Absorbed pump shaft power in \(\text{kW}\)
\(P_0\) = Reference power standard = \(1\text{ kW}\)
2.4 STEP 4 : Convert Sound Power Level \(L_{wA}\) to Sound Pressure Level \(L_p\) at Distance
In industrial plant layouts, acoustic sensors or worker ear levels measure the Sound Pressure Level \(L_p\) at a specified distance \(r\) (typically 1 meter). In a semi-free acoustic field over a rigid reflective concrete foundation (hemispherical propagation with directivity factor \(Q = 2\)), the relationship is:
🏭 Practical Plant Engineering Rules of Thumb & Safety Limits
Occupational Limits (OSHA 1910.95 & EU 2003/10/EC): Sound pressure levels at 1 meter exceeding 85 dB(A) trigger mandatory hearing protection, noise mapping, and occupational surveillance. Sound levels exceeding 90 dB(A) necessitate engineered acoustic shrouds or enclosures.
Cavitation Acoustic Fingerprint: Cavitation noise does not follow the empirical power formulas above! It generates broadband high-frequency acoustic emission resembling rattling chains, gravel, or shaking marbles inside the casing. Cavitation accelerates impinging erosion and can raise noise levels by 10 to 18 dB(A) above nominal baseline.
Liquid Suction Velocity: Keep pump suction liquid velocity between 1.0 and 1.8 m/s (3.3 to 6 ft/s) to avoid vortex generation and pre-rotation turbulence. Pump discharge lines should operate within 2.0 to 3.0 m/s (6.5 to 10 ft/s).
Straight Pipe Run at Suction: Maintain a minimum of 5 to 10 pipe diameters (\(5D\) to \(10D\)) of straight, unobstructed pipe upstream of the pump suction flange. Eliminating eccentric reducers with the flat side on bottom and avoiding short-radius elbows in the vertical plane directly before the suction nozzle will prevent asymmetric impeller loading and turbulent noise.
Vibration Isolation & Baseplates: Always secure pump and driver on a rigidly grouted baseplate. Utilize elastomeric vibration isolators or stainless steel flexible expansion bellows on suction and discharge flanges when piping resonance is detected.
3. Noise control : reduction for pumps
How to make a pump less noisy ?
3.1 Noise reduction by design
Accurate hydraulic design is the first line of defense. Selecting an oversized pump forces the operating point to the left of the Best Efficiency Point (BEP). Operating in this low-flow zone induces internal hydraulic recirculation at the impeller inlet and discharge tips, creating strong structural vibration and hydrodynamic noise. Best practices include:
Low Flow Velocity: Size suction and discharge pipe diameters generously to maintain conservative fluid velocities.
Low Noise Fittings: Install long-radius elbows (\(R \ge 1.5D\)) rather than short-radius fittings, and avoid concentric reducers in horizontal suction lines (use eccentric reducers flat-on-top to eliminate air pockets).
Structural Damping: Mount the motor-pump skid on a mass-concrete inertial foundation with epoxy grout and vibration-damping neoprene/spring mounts.
Low Noise Drivers: Standard totally enclosed fan cooled (TEFC) electric motors frequently generate aerodynamic fan whistle. Use low-noise aerodynamic fans, variable speed drives (VFDs) running at lower rpm, or acoustic motor baffles.
Special case of cavitation:
A pump experiencing acoustic cavitation must be addressed immediately. Ensure that the Net Positive Suction Head Available (\(\text{NPSH}_a\)) exceeds the vendor Net Positive Suction Head Required (\(\text{NPSH}_r\)) by at least a 0.6 m to 1.0 m (or 20% to 25%) safety margin under all operating temperatures. Check our detailed guide: NPSH and Cavitation Troubleshooting.
3.2 Noise reduction by insulation
When hydraulic redesign or motor substitution is unfeasible, install acoustic enclosures constructed of mineral wool absorption cores backed by galvanised steel sheeting. Ensure the enclosure provides forced acoustic labyrinth ventilation to prevent motor overheating, along with quick-release access hatches for mechanical seal inspections and vibration monitoring.
4. Field Troubleshooting: Practical Tips & Tricks
Field process engineers encountering pump issues can troubleshoot common symptoms using the following systematic checks:
Pump Suction Head & Starting NPSH: Always vent air from the pump casing and prime the suction line before starting. Starting a centrifugal pump against an air pocket can cause cavitation-like hammer, dry seal running, and severe vibration.
Measuring Motor Amperage: High running amps indicate operation too far right on the H-Q curve (excessive flow and motor overload), high specific gravity liquid, or mechanical binding. Low amps with zero flow indicates internal air-lock, closed isolation valves, or backward impeller rotation.
Direction of Rotation: Three-phase electric motors can easily run in reverse if wiring polarity is switched. A centrifugal pump rotating backwards will still pump liquid, but with significantly reduced head (typically 30–50% of nominal) and an abnormally loud hydraulic drone. Verify the motor rotation arrow prior to coupling the shaft.
Hot Motor Casing: A hot motor casing can result from excessive ambient temperature, high start/stop cycle frequency, clogged cooling air cowls, low voltage causing elevated current, or improper coupling alignment transmitting axial thrust into the motor bearings.
Energy Savings & Extended Seal Life: Throttling a discharge control valve wastes significant electrical energy across the valve and shifts the pump into the noisy recirculation zone. Trimming the impeller diameter or implementing a Variable Frequency Drive (VFD) saves energy while slashing acoustic pressure and bearing loads.
5. Manufacturers & References
For specialized acoustic specifications, low-noise impellers, or certified noise emission guarantees, consult certified pump vendors:
Flowserve, Sulzer, and KSB: Industrial single-stage and heavy multi-stage API 610 / ISO process pumps with full acoustic documentation.
Sterling Sihi (Flowserve Sihi): Side channel liquid pumps, multi-stage pumps, and liquid ring vacuum machinery.
Grosclaude: Chemical centrifugal pump equipment.
Note: MyEngineeringTools has no commercial affiliation with the companies referenced.
Acoustic Bibliography & References:
[Sihi] Basic Principles for the Design of Centrifugal Pumps Installations, Sterling Sihi GmbH, 2003.
[ISO 3744 / 3746] Acoustics — Determination of sound power levels and sound energy levels of noise sources using sound pressure.
[API 610] Centrifugal Pumps for Petroleum, Petrochemical and Natural Gas Industries, American Petroleum Institute.