1 kPa difference
- Liquid head
- 101.972 mm
- Pressure difference
- 1 kPa
- Bar
- 0.01 bar
More dimensions
- Entered liquid density
- 1,000 kg/m³
VALICALC · TECHNICAL REFERENCE
Compare pressure in kPa, bar and psi with hydrostatic head at an editable liquid density. Keep pressure difference separate from pipe friction and elevations.
ValiCalc · Water Pressure & Head Reference
https://www.valicalc.com/water-pressure-head-reference
Dataset v1.3.0 · verified 2026-10-07
Display: metric. Liquid density: 1000 kg/m³
Search within the verified subset. Numeric sizes match complete designations; a nearby size is a candidate, not an exact match.
SELECTED REFERENCE
v1.3.0 · verified 2026-10-07 · values use the valid conditions shown above
9 matching rows · 9 in this subset
| Pressure difference scenario | Liquid head | Pressure difference | Bar | Actions |
|---|---|---|---|---|
| 1 kPa difference | 101.972 mm | 1 kPa | 0.01 bar | |
| 10 kPa difference | 1,019.716 mm | 10 kPa | 0.1 bar | |
| 25 kPa difference | 2,549.291 mm | 25 kPa | 0.25 bar | |
| 50 kPa difference | 5,098.581 mm | 50 kPa | 0.5 bar | |
| 100 kPa difference | 10,197.162 mm | 100 kPa | 1 bar | |
| 200 kPa difference | 20,394.324 mm | 200 kPa | 2 bar | |
| 300 kPa difference | 30,591.486 mm | 300 kPa | 3 bar | |
| 500 kPa difference | 50,985.811 mm | 500 kPa | 5 bar | |
| 1000 kPa difference | 101,971.621 mm | 1,000 kPa | 10 bar |
h[m]=Δp[Pa]/(ρg). Store head in canonical mm; pressure in kPa. 1bar=100kPa; psi display uses exact customary-unit definitions.
CHECK THE METHOD
100 kPa at 1000 kg/m³ gives 10.19716 m liquid head. At lower density the same pressure requires more head.
Hydrostatic pressure head is one term in TDH. It is not total pump duty, gauge datum, available NPSH or a pressure-rating check; confirm liquid density and boundary pressures.
TRACEABLE DATA
Dataset v1.3.0
Last verified:
Nine authored pressure-difference scenarios using g = 9.80665 m/s², not a fixed universal metres-per-bar value for every fluid.
Values are curated product facts or generated scenarios. Paid standards, complete catalogs and source diagrams are not reproduced. A verification date applies to this documented subset.
Type A · NIST · SP 1038, 2006; exact definitions used where available
Original equations, chosen scenarios and generated values; no copied tables or drawings.