Calculators › Control Valve Noise Calculator
🔊

Control Valve Noise Calculator

IEC 60534-8-3 Aerodynamic Noise Prediction

Control Valve Noise Prediction (IEC 60534-8-3)
Predict aerodynamic noise from control valves in gas, steam, or liquid service. Calculates sound pressure level at a specified distance, determines OSHA compliance, identifies noise regime (subsonic vs. choked), and recommends noise mitigation when levels exceed 85 dBA. Supports standard, low-noise, and anti-cavitation trim types.

Service Conditions

psig
psig
°F

Flow Conditions

lb/hr
lb/lbmol

Natural gas ~18.5, Air ~29, Steam ~18

-

Natural gas ~1.27-1.31, Air ~1.4, Steam ~1.3

Valve Configuration

inches
-

Downstream Piping

inches
ft

Standard: 3.28 ft (1 meter) from pipe wall

Understanding Control Valve Noise

Aerodynamic Noise
In gas/steam service, turbulent mixing and shock waves at the vena contracta generate broadband noise. Sound power increases sharply when the pressure ratio exceeds the critical value xT (choked flow).
Hydrodynamic Noise
In liquid service, cavitation occurs when local pressure drops below vapor pressure. Vapor bubble collapse produces high-frequency noise and can damage trim and body. The cavitation index sigma determines severity.
OSHA Limits (29 CFR 1910.95):
85 dBA = hearing conservation program required | 90 dBA = 8-hour permissible exposure limit | 100 dBA = 2-hour limit | 115 dBA = 15-minute limit. Each 5 dB increase halves the allowable exposure time.

📚 Learn the Theory

Understand noise mechanisms, IEC prediction method, pipe wall transmission loss, and noise reduction techniques

Read Engineering Guide →

Formula

SPL = Lw − TL − 10·log(2πrL)
SPL = Sound pressure level at distance r (dB)
Lw = Sound power level (dB)
TL = Pipe wall transmission loss (dB)
r = Distance from pipe wall (m)
L = Effective radiating pipe length (m)
x = (P1−P2)/P1 (pressure ratio)
xT = Critical pressure ratio (valve-specific)

Standards & References

  • IEC 60534-8-3
    Control Valve Aerodynamic Noise Prediction
  • ISA 75.17 (ANSI/ISA-75.17)
    Control Valve Aerodynamic Noise Prediction
  • OSHA 29 CFR 1910.95
    Occupational Noise Exposure Limits
  • IEC 60534-8-4
    Hydrodynamic Noise Prediction (Liquid)
  • GPSA Engineering Data Book
    Section 7: Control Valves

Engineering Notes

  • Choked flow: When x > xT, flow is choked and noise increases rapidly. Globe valves have higher xT (~0.7) than ball valves (~0.15).
  • Low-noise trim: Multi-hole cage trims reduce noise 10-15 dB by dividing flow into small streams and shifting peak frequency higher.
  • Anti-cavitation trim: Multi-stage pressure reduction prevents cavitation in liquid service, reducing noise and protecting trim.
  • Pipe schedule: Heavier wall pipe provides greater transmission loss, reducing external noise by 3-8 dB.
  • Distance effect: SPL decreases ~6 dB per doubling of distance from the pipe surface.
  • A-weighting: Results are A-weighted (dBA) to match human hearing sensitivity. Low frequencies are attenuated relative to mid-range.

Quick Reference — Typical xT Values

  • Globe valve (parabolic plug): xT = 0.70
  • Globe valve (V-port): xT = 0.65
  • Cage-guided globe: xT = 0.65-0.75
  • Ball valve (full bore): xT = 0.15
  • Ball valve (V-notch): xT = 0.25
  • Butterfly valve: xT = 0.25-0.35

Related Calculators

🔧

Control Valve Sizing

Size Cv for gas, liquid, or steam per ISA/IEC standards
🔴

Relief Valve Sizing

Size relief valves per API 520/521
📏

Line Sizing

Gas and liquid line sizing with velocity limits
⚗️

Gas Density

Calculate gas density at operating conditions