Size minor losses with confidence. Compare methods, validate inputs, and export results. Make hydraulic estimates clearer for daily engineering work.
This graph shows how head loss changes with velocity for the current or default coefficient.
| Component | Velocity (m/s) | Head Loss (m) | Density (kg/m³) | Estimated K |
|---|---|---|---|---|
| Sharp 90° elbow | 2.20 | 1.80 | 998 | 7.2967 |
| Swing check valve | 2.60 | 2.40 | 998 | 6.9657 |
| Sudden contraction | 3.10 | 3.00 | 997 | 6.1249 |
| Tee through branch | 1.75 | 1.50 | 999 | 9.6098 |
Minor losses in pipes, valves, bends, tees, and fittings are commonly represented with a dimensionless loss coefficient, K.
hL = K × (V² / 2g)Where hL is head loss, K is loss coefficient, V is mean velocity, and g is gravity.
K = hL / (V² / 2g)Use this form when measured or estimated head loss is already known.
ΔP = ρghLPressure drop can be converted into head loss with fluid density and gravity.
K = f × (L / D)This approximation converts equivalent fitting length into a minor loss coefficient.
These equations are useful for hydraulic modeling, HVAC piping, pump sizing, process systems, water distribution, and industrial flow network checks.
For best results, keep units consistent. Use SI units throughout, especially for diameter, flow rate, density, pressure, and head values.
It measures how much energy a fitting or component removes from flowing fluid. A higher coefficient means greater local resistance and more head loss.
Yes. K is dimensionless because it compares actual energy loss with velocity head. That makes it useful across many flow situations when units stay consistent.
Use it when test data, manufacturer information, or hydraulic calculations already provide local head loss for the component being evaluated.
Yes. Convert pressure drop to head loss using density and gravity. The calculator handles this automatically in pressure-drop mode.
Head loss is proportional to velocity squared. Small increases in flow speed can create noticeably larger local losses in fittings and bends.
It replaces a fitting with an imaginary pipe length producing the same frictional effect. From that length, you can estimate an approximate K value.
Yes, for many engineering estimates. Still, compressibility, temperature, and high-speed effects may require more advanced analysis for gas systems.
Values change with geometry, Reynolds number, opening position, surface condition, and test method. Treat handbook values as design estimates unless verified experimentally.
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.