โš ๏ธ Safety & Relief Valve Sizing

Size pressure relief valves (PRV) for gas, vapor, steam, or liquid service per API 520, and select the standard API 526 orifice designation.

โšก Fortran 90 Engine Double Precision (IEEE 754) โœ“ ISO / ASME Validated
Safety & Relief Valve Sizing Tools
๐Ÿ“Š Solver Telemetry โ— ACTIVE
๐Ÿ‘๏ธ Views 3,640
โšก Solves 2,906
๐Ÿ’พ Downloads 489 ๐Ÿ“ฆ Fortran Code 4.4 KB
๐Ÿ“… Released Jun 2026
โฑ๏ธ Latency < 1 ms
โšก TOOLS & REPORTS:
๐Ÿ’พ Download Fortran 90
๐Ÿ’ก Hardware & Sizing Partner: Need to size a control valve or check ASME flange bolt torque for this line?
FLOWKS IEC 60534 Sizer โ†— API 6D Valve Catalog →

๐Ÿ“ Configuration

โš™๏ธ Service

๐Ÿ“Š Results

Configure inputs and click Size.

๐Ÿ“˜ Methodology

API 520 Gas/Vapor

A = Wยทโˆš(TZ/(Mk)) / (CยทKdยทP1ยทKb). The coefficient C depends on the isentropic exponent k. Kd is the discharge coefficient (0.975 for gas). Kb corrects for backpressure.

API 520 Steam & Liquid

Steam: A = W/(51.5ยทKdยทP1ยทKnยทKsh). Liquid: A = Qยทโˆš(ฯ/ฮ”P)/(38ยทKdยทKwยทKv). Each service type uses specific correction factors per the standard.

API 526 Orifice Designations

Standard orifice letters D through T define discrete valve sizes from 71 mmยฒ to 16,774 mmยฒ. The selected orifice must equal or exceed the calculated required area.

๐Ÿ“˜ Calculation Methodology: API 520 Pressure Relief Valve (PRV) Sizing

Mathematical Model & Theory

Sizes safety relief valves for vapor/gas and liquid emergency overpressure relief per API 520 Part I standards, calculating required effective discharge area $A$:

$$A = \frac{W}{C K_d P_1 K_b K_c} \sqrt{\frac{T Z}{M}} \quad (\text{Vapor/Gas}), \quad A = \frac{Q}{38 K_d K_w K_v} \sqrt{\frac{G}{\Delta P}} \quad (\text{Liquid})$$
$$P_1 = \text{Set Pressure} \times (1 + \text{Overpressure Fraction}) + P_{atm}$$

Assumptions

  • Critical acoustic choked nozzle flow across orifice.
  • Discharge coefficient $K_d = 0.975$ for certified ASME Section VIII relief valves.

Academic References

  1. API Standard 520 Part I: Sizing, Selection, and Installation of Pressure-relieving Devices, 10th Edition.
  2. ASME Boiler and Pressure Vessel Code: Section VIII Division 1.

Worked Engineering Example

Problem Statement:
Size a PRV for natural gas ($M = 18\text{ g/mol}$, $Z = 0.95$, $T = 310\text{ K}$, $k = 1.30 \implies C = 345$) relieving mass flow $W = 15,000\text{ kg/h}$ ($33,069\text{ lb/h}$) at relieving pressure $P_1 = 12.0\text{ bar, abs}$ ($174\text{ psia}$), $K_d = 0.975, K_b = 1.0$. Find required orifice area.

Step-by-step Solution:
1. Calculate required area $A$ in standard API units (or metric):
$$A \approx 942\text{ mm}^2 = 1.46\text{ in}^2$$
2. Select standard API orifice letter: **\"J\" Orifice** (Standard area $A = 1.287\text{ in}^2$) or **\"K\" Orifice** ($A = 1.838\text{ in}^2 = 1186\text{ mm}^2$).
Final Result:
Required effective discharge area is $\mathbf{942\text{ mm}^2}$ (Select **API 520 \"K\" Letter Orifice**).