Hydrostatic Test Pressure
Two different tests that get confused with each other: the factory shell test on a flange, and the field leak test on a completed system. Both worked through with tables.
- B16.5 shell test
- 1.5 × the 100 °F rating
- B31.3 hydrotest
- 1.5 × design pressure, stress adjusted
- Minimum hold time
- 10 minutes, then examine
- Rounding
- Up to the next 25 psi increment
Short answer. Two different test pressures get confused with each other. The shell test in ASME B16.5 is a factory proof test on the flange itself, at 1.5 times the 100 °F rating of its class and material group. The hydrostatic leak test in ASME B31.3 is a field test on the completed system, at 1.5 times the design pressure, adjusted upward when the test temperature is colder than the design temperature.
The B16.5 shell test
Every flanged fitting is proof tested at the works before it ships. B16.5 sets that pressure at 1.5 times the ambient rating for the class and material group, rounded up to the next 25 psi increment. It is a one-off structural proof, not a leak test of a gasketed joint — the flange is tested as a pressure-containing shell.
Shell test = 1.5 × (rating at 100 °F), rounded up to the next 25 psi
| Material group | Class 150 | Class 300 | Class 400 | Class 600 | Class 900 | Class 1500 | Class 2500 |
|---|---|---|---|---|---|---|---|
| Group 1.1 | 285 | 740 | 990 | 1480 | 2220 | 3705 | 6170 |
| Group 1.2 | 265 | 695 | 925 | 1390 | 2085 | 3470 | 5785 |
| Group 2.1 | 275 | 720 | 960 | 1440 | 2160 | 3600 | 6000 |
| Group 2.2 | 275 | 720 | 960 | 1440 | 2160 | 3600 | 6000 |
These are the ambient ratings for each material group. See the full P-T rating tables for the temperature curves.
| Material group | Class 150 | Class 300 | Class 400 | Class 600 | Class 900 | Class 1500 | Class 2500 |
|---|---|---|---|---|---|---|---|
| Group 1.1 | 450 | 1125 | 1500 | 2225 | 3350 | 5575 | 9275 |
| Group 1.2 | 400 | 1050 | 1400 | 2100 | 3150 | 5225 | 8700 |
| Group 2.1 | 425 | 1100 | 1450 | 2175 | 3250 | 5400 | 9000 |
| Group 2.2 | 425 | 1100 | 1450 | 2175 | 3250 | 5400 | 9000 |
Computed from the ratings in the table above. Confirm against ASME B16.5 Table F2 before using these for acceptance.
The B31.3 system hydrotest
Once the system is built, ASME B31.3 paragraph 345.4.2 requires a hydrostatic leak test at not less than 1.5 times the design pressure. Where the design temperature is above the test temperature — which it almost always is — the test pressure is raised by the ratio of allowable stresses, because the material is stronger cold than it will be hot:
PT = 1.5 × P × (ST / S)
ST = allowable stress at test temperature · S = allowable stress at design temperature
The ratio ST/S is capped at 6.5, and the test pressure must not produce a stress above the material's yield point at test temperature — which is what actually limits it in practice on a hot line.
Worked example
A Class 300 carbon steel line, design pressure 500 psig, design temperature 650 °F, tested with water at ambient.
- Base test pressure: 1.5 × 500 = 750 psig
- Allowable stress for A106 Gr B: 20,000 psi at 100 °F and 17,300 psi at 650 °F, so ST/S = 1.156
- Corrected test pressure: 750 × 1.156 = 867 psig
- Check against the flange: a Class 300 Group 1.1 flange is rated 740 psig at 100 °F, so 867 psig is within it and the flanges do not limit the test.
That last check is the one that gets missed. If the corrected test pressure exceeds the ambient rating of any flange, valve or component in the test envelope, the test cannot proceed at that pressure — either the component is removed and blanked, or the test is split into sections, or a lower test pressure is agreed with the owner under the code's provisions.
Practical requirements
| Requirement | ASME B31.3 provision |
|---|---|
| Minimum hold time | 10 minutes at test pressure, after which the pressure may be reduced to the design pressure for examination. |
| Test fluid | Water unless there is a risk of damage from freezing or from adverse effects on the piping material. |
| Water chemistry | Chloride content is limited for austenitic stainless — commonly 50 ppm or less — to avoid stress corrosion cracking. Drain and dry promptly. |
| Test temperature | Kept above the material's ductile-brittle transition. Testing carbon steel with cold water on a cold day is a real brittle fracture risk. |
| Venting | The system must be vented at high points while filling. Trapped air stores energy and makes a failure violent. |
| Pneumatic testing | Permitted only where hydrostatic testing is impracticable, and requires a documented hazard assessment — stored energy in a gas test is orders of magnitude higher. |
Paraphrased for orientation. The governing code text prevails — confirm against a current copy before planning a test.
See also: P-T rating tables · how derating works · blanking with blind flanges · bolt torque.
Common questions
What is the hydrostatic test pressure for a Class 150 flange?
The B16.5 shell test for a Group 1.1 Class 150 flange is 450 psig — 1.5 times the 285 psig ambient rating, rounded up to the next 25 psi. That is a works proof test, not the field system test.
How is the B31.3 hydrotest pressure calculated?
1.5 times the design pressure, multiplied by the ratio of allowable stress at test temperature to allowable stress at design temperature. The ratio is capped at 6.5 and the result must not yield the material.
How long must a hydrostatic test be held?
ASME B31.3 requires at least 10 minutes at the test pressure. The pressure may then be reduced to the design pressure while the joints are examined for leakage.
Why is chloride limited in stainless steel test water?
Because residual chlorides concentrate as the system dries and can initiate stress corrosion cracking in austenitic stainless. A limit around 50 ppm is common, with prompt draining and drying required.
Can I pneumatically test instead of hydrostatically?
Only where a hydrostatic test is impracticable — for example where the system cannot take the water weight or traces of water are unacceptable. A gas test stores vastly more energy and requires a documented hazard assessment.