How to Size a Relief Valve: API 520
Pressure relief valve sizing per API 520 Part I determines the minimum effective discharge area (orifice area) required to relieve a specified mass or volume flow rate at a given set pressure. The calculated area is matched to a standard API orifice letter designation, and the valve inlet and outlet sizes are selected accordingly.
When This Calculation Is Used
Process safety engineers size relief valves for every pressure vessel and piping system that can be exposed to overpressure. Common relieving scenarios include fire case, blocked outlet, thermal expansion, control valve failure, and tube rupture. API 520 Part I covers sizing; API 521 defines the relieving scenarios; API 526 standardizes the orifice sizes.
API 520 Orifice Area Formula (Gas/Vapor)
A = W / (C x K x P1 x Kb x Kc) x sqrt(T x Z / M)
| Symbol | Parameter | Unit |
|---|---|---|
| A | Required effective discharge area | in2 |
| W | Required relieving rate | lb/hr |
| C | Gas constant coefficient (function of k = Cp/Cv) | Dimensionless |
| K | Effective coefficient of discharge (0.975 for API-certified valves) | Dimensionless |
| P1 | Relieving pressure (set pressure x 1.10 + atmospheric) | psia |
| Kb | Back-pressure correction factor | Dimensionless (1.0 for conventional; < 1.0 for balanced bellows) |
| Kc | Combination correction factor (1.0 without rupture disc; 0.9 with) | Dimensionless |
| T | Relieving temperature | Rankine (F + 460) |
| Z | Gas compressibility factor at relieving conditions | Dimensionless |
| M | Molecular weight of gas | lb/lb-mol |
API 520 Orifice Area Formula (Liquid)
A = Q / (38 x K x Kw x Kv) x sqrt(G / (P1 - P2))
Where Q is in US GPM, G is specific gravity, P1 is set pressure x 1.10 + atmospheric (psia), and P2 is total back pressure (psia).
Standard API 526 Orifice Designations
| Letter | Effective Area (in2) | Effective Area (mm2) | Typical Inlet x Outlet |
|---|---|---|---|
| D | 0.110 | 71.0 | 1” x 2” |
| E | 0.196 | 126.5 | 1” x 2” |
| F | 0.307 | 198.1 | 1.5” x 2.5” |
| G | 0.503 | 324.5 | 1.5” x 3” |
| H | 0.785 | 506.5 | 2” x 3” |
| J | 1.287 | 830.3 | 3” x 4” |
| K | 1.838 | 1,186 | 3” x 4” |
| L | 2.853 | 1,841 | 4” x 6” |
| M | 3.600 | 2,323 | 4” x 6” |
| N | 4.340 | 2,800 | 4” x 6” |
| P | 6.380 | 4,116 | 4” x 6” or 6” x 8” |
| Q | 11.05 | 7,129 | 6” x 8” or 6” x 10” |
| R | 16.00 | 10,323 | 6” x 10” or 8” x 10” |
| T | 26.00 | 16,774 | 8” x 10” |
Sizing Steps
- Identify all overpressure scenarios per API 521 (fire, blocked outlet, thermal expansion, etc.)
- Calculate the required relieving rate (W or Q) for each scenario
- Apply the appropriate API 520 formula (gas, liquid, steam, or two-phase)
- Select the smallest standard API 526 orifice letter that provides an effective area equal to or greater than the calculated area
- Verify inlet pressure drop does not exceed 3% of set pressure (API 520 Part II)
- Verify that the back pressure is within the valve’s allowable range
For information on safety and pressure relief valve types and their applications in piping systems, see the detailed reference guide.
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