Documented Pressure-Relief Area Comparison Worksheet
Compare one required effective discharge area from an approved governing calculation with one compatible certified candidate area. The two values must describe the same relief case, fluid regime, coefficient basis and unit.
Controlled comparison record
Enter areas only after a competent calculation and a certified manufacturer record have established a compatible basis.
Arithmetic comparison result
Formula and model boundary
For positive compatible effective areas expressed in one shared unit:
Q, U and δ are dimensionless; ΔA retains the selected area unit. These identities do not establish a relief load, discharge capacity or regulatory acceptance criterion.
Why the former sizing formulas and presets were removed
The previous page combined gas/vapour and steam, assumed fixed discharge coefficients, invented a generic back-pressure factor, used a fixed 10% overpressure and treated water density as universal. It did not control critical versus subcritical flow, phase behaviour, certified coefficient basis, inlet losses, built-up and superimposed back pressure, viscosity/two-phase behaviour, installation or jurisdiction. Those omissions can change a required area materially and cannot be repaired by relabelling one simplified equation.
API 520 Part I and the relevant ISO 4126 parts are controlled standards with application-specific procedures and data. Their closed equations, coefficients and tables are not reproduced or inferred here. A competent engineer with the licensed governing documents and manufacturer data must produce Areq and verify Acert.
Exact numerical checks
| Masukan | Q | U | ΔA | δ |
|---|---|---|---|---|
| Areq=100 mm²; Acert=120 mm² | 1.2 | 83.3333333333% | 20 mm² | 20% |
| Areq=0.5 in²; Acert=0.75 in² | 1.5 | 66.6666666667% | 0.25 in² | 50% |
Official source status and classification
| Sumber | Current public status inspected | Use on this page |
|---|---|---|
| API Standard 520 Part I | 10th edition, published 2020-10-28; official API title is sizing and selection of pressure-relieving devices in refineries | Scope/lifecycle only. No formula or coefficient is copied. |
| API Standard 526 | 8th edition, published 2023-08-14; flanged steel pressure-relief valves | No built-in orifice-letter table. Use the controlled current standard and manufacturer record. |
| ISO 4126-1:2013 + Amd 1:2016 | Edition 3, published and confirmed in 2025 | The official abstract calls Part 1 a product standard and says it is not applicable to applications of safety valves. |
| ISO 4126-7:2013 + Amd 1:2016 | Edition 2, published and confirmed in 2025 | Common data for Parts 1–6; licensed content is required for technical use. |
| ISO 4126-9:2008 | Edition 1, published and confirmed in 2026 | Application/installation of safety devices for static pressure equipment; its public scope assumes single-phase discharge and points two-phase conditions to ISO 4126-10. |
API 520 Part I official announcement · API official standards plan · ISO 4126-1 official card · ISO 4126-7 official card · ISO 4126-9 official card
Accessed: 15 July 2026. Licensed-source boundary: NEEDS_LICENSED_SOURCE for every sizing equation, coefficient, correction, allowable-overpressure rule, standardized orifice table and acceptance criterion. None was guessed from a search snippet or another online calculator.