| 1 | Confirm the nominal pressure class | Common PVC butterfly valve pressure classes include PN10 and PN16, equivalent to approximately 10 bar (145 psi) and 16 bar (232 psi) nominal pressure. | PN10: 10 bar (145 psi)
PN16: 16 bar (232 psi) | These values are normally reference ratings near room temperature. The allowable pressure generally decreases as temperature rises. | Choose a valve whose derated pressure rating exceeds the highest continuous operating pressure, including expected surges where applicable. | Check whether the rating applies to the complete valve assembly or only to the body material. |
| 2 | Compare pressure ratings at the actual operating temperature | Representative PVC-U derating factors for pressure applications: | At 23°C: 100% of reference rating | 27°C: approximately 87% 32°C: approximately 75% 38°C: approximately 62% 43°C: approximately 50% | For a PN10 valve, a 50% factor corresponds to approximately 5 bar (72.5 psi), before any additional limits from seals, discs, flanges, or actuator components. | Use the valve supplier’s published pressure-temperature curve when available; generic PVC pipe factors are not a substitute for a valve rating. |
| 3 | Respect the upper temperature limit | PVC-U is commonly selected for ambient and moderately warm liquid service, but its pressure capability declines significantly with heat. | Full reference rating is generally associated with approximately 23°C (73°F) | 49°C: approximately 40% 54°C: approximately 30% 60°C: approximately 20% Above 60°C: application-specific review required | Do not treat a PVC valve as a full-pressure valve at elevated temperature. Hot water, solar-heated fluids, and process liquids require a dedicated temperature review. | Confirm the maximum continuous and intermittent temperature, not only the normal operating temperature. |
| 4 | Match the valve material to the fluid | PVC-U is commonly compatible with many water, salt-water, dilute acid, alkali, and some chemical services, but compatibility depends on concentration, temperature, and exposure time. | Pressure rating does not establish chemical compatibility | Higher temperature can accelerate chemical attack, permeation, swelling, or seal degradation even when the pressure derating appears acceptable. | Review the body, disc, shaft, liner, seat, and elastomer separately. EPDM and FKM, for example, have different chemical and temperature behavior. | Obtain a chemical-compatibility confirmation for the exact concentration and operating temperature. |
| 5 | Select the correct size and flow arrangement | Common nominal sizes range from small utility lines to large process pipelines. Butterfly valves are generally suited to isolation and throttling service when the design permits. | Pressure class may remain constant across sizes, but the actual design limits can vary by size and connection style | Temperature derating applies to the selected size and complete construction; large discs, liners, and flanges may introduce additional limits. | Avoid selecting a valve solely by pipe diameter. Check flow coefficient, velocity, pressure drop, disc clearance, and required shutoff performance. | Confirm wafer, lug, or flanged pattern, face-to-face dimensions, flange drilling, and pipe schedule. |
| 6 | Account for installation and pressure direction | Butterfly valves can be sensitive to pipe alignment, flange spacing, bolt tightening, and disc clearance during installation. | Rated pressure assumes correct installation and a properly supported piping system | Elevated temperature increases thermal expansion and can increase mechanical stress at joints, flanges, and supports. | Align the pipe before tightening, prevent the disc from striking the pipe, use the specified gasket arrangement, and follow the correct bolt-torque procedure. | Check the permitted pressure direction, end connections, support requirements, and any vacuum-service limitations. |
| 7 | Include safety margin and testing requirements | Operating pressure should remain below the temperature-adjusted working-pressure rating. Hydrostatic testing pressure must follow the applicable standard and project specification. | Design condition must be lower than the derated working rating | Never multiply a published rating by a generic factor without confirming the rating basis, test standard, and component limitations. | Consider start-up, shutdown, water hammer, pump transients, vacuum conditions, and cyclic temperature changes before final selection. | Verify applicable standards, inspection requirements, leakage class, pressure-test procedure, and documentation for the installed valve. |