| General liquid or gas service | Bourdon-tube gauge | Select a full-scale range so normal operating pressure is approximately 25%–75% of full scale. | Install where the dial is visible. Use a shut-off valve or gauge valve to allow safe isolation and removal. | Common industrial accuracy classes include approximately ±1.0% or ±0.5% of full scale. Calibrate at commissioning and at an interval based on risk and history. | Inspect the case, window, pointer, dial, connection, and leakage condition. Compare periodically with a traceable reference. | Suitable for stable, non-corrosive service |
| Pressure with pulsation or vibration | Liquid-filled gauge or gauge with a pulsation dampener | Keep normal pressure within the middle portion of the scale and avoid continuous operation near full scale. | Use a snubber, restrictor, or dampener where rapid cycling may damage the sensing element. Provide mechanical support for vibrating pipework. | Check zero return and pointer stability after installation. Shorten the calibration interval if cycling causes measurable drift. | Look for foaming, discoloration, leakage, loose fittings, and abnormal pointer movement. Replace damaged dampening components. | Recommended for cycling or vibrating systems |
| Steam or high-temperature process | Bourdon-tube gauge with a siphon or cooling element | Choose a range that keeps normal pressure near the center of the dial while allowing for start-up and upset conditions. | Install a properly filled siphon before commissioning. Confirm that the gauge temperature rating is compatible with the process. | Calibrate after the installation has reached normal operating conditions if temperature can affect the reading. | Verify that the siphon remains filled and is not blocked. Isolate and cool the system before removing the gauge. | Required where process temperature exceeds gauge limits |
| Corrosive, viscous, or contaminated medium | Diaphragm-sealed gauge or gauge with compatible wetted materials | Size the range for the actual process pressure and consider the effect of seal fill fluid and temperature. | Use wetted materials compatible with the medium. Avoid dead legs and install flushing connections where deposits are expected. | Check calibration with the seal system installed; do not expose the sensing diaphragm to incompatible cleaning chemicals. | Inspect the diaphragm seal, capillary, flushing ports, and process connection for corrosion, blockage, or leakage. | Preferred for difficult or chemically aggressive media |
| Low-pressure measurement or differential pressure | Diaphragm, capsule, or differential-pressure gauge | Use the lowest practical full-scale range that covers the maximum permissible operating pressure without over-ranging. | Connect high- and low-pressure ports correctly. Protect low-pressure instruments from static pressure and excessive differential pressure. | Zero-check both ports at equal pressure where applicable. Calibrate at several points across the working range. | Check impulse lines for blockage, condensation, air pockets, and unequal liquid head. Verify both isolation valves and equalizing valves. | Suitable when differential pressure is the measured variable |
| Oxygen or other oxidizing service | Gauge specifically cleaned and prepared for the service | Select a range that avoids frequent operation near the upper limit and accommodates expected pressure transients. | Use service-compatible fittings and ensure all components are free from oil, grease, and other contaminants. Follow applicable oxygen-service procedures. | Use a calibration method and reference instrument approved for the service. Preserve cleanliness after calibration. | Do not use contaminated gauges. Inspect packaging, connection cleanliness, seals, and protective caps before installation. | Requires dedicated cleanliness controls |
| Hazardous or personnel-critical service | Safety-pattern gauge with suitable pressure protection | Choose a range that accommodates normal and abnormal pressure while maintaining readable resolution. | Use a suitable isolation valve, pressure-limiting device, and safe venting arrangement. Position the gauge away from direct exposure to personnel where required. | Set a documented calibration interval according to regulatory, safety, and process requirements. Record as-found and as-left results. | Perform visual checks, leak checks, functional verification, and documented replacement when damage or drift exceeds the permitted tolerance. | Requires formal inspection and records |
| Outdoor, wet, dusty, or corrosive environment | Weather-resistant gauge with suitable enclosure and materials | Allow sufficient range margin for ambient temperature effects and transient pressure conditions. | Use an appropriate mounting position, drain or vent provisions where applicable, and compatible seals. Prevent water from collecting at the connection. | Check for temperature-related zero shift and environmental damage during calibration. | Inspect the window, case, seal, connection, corrosion protection, and mounting hardware. Replace cracked windows or compromised seals. | Suitable when environmental protection is verified |
| Commissioning and initial verification | Gauge selected for the process and verified against a reference | Confirm the scale, pressure unit, connection size, pressure rating, and range before applying pressure. | Check piping cleanliness, correct thread engagement, seal compatibility, orientation, isolation, and leak tightness. Tighten using the connection flats, not the case. | Record the serial or asset identifier, reference standard, test points, environmental conditions, and results. | Establish a baseline zero reading and compare the gauge at several pressure points before placing it into service. | Required before operational acceptance |
| Routine calibration planning | Existing gauge assessed according to service criticality | Review whether the installed range still matches current operating pressure and process changes. | Isolate, depressurize, and make the gauge safe before removal or testing. Use a suitable test pump and reference standard. | Annual calibration is a common starting point, but the interval should be adjusted using drift history, risk, usage, and applicable requirements. | Trend as-found errors. Shorten the interval after excessive drift; extend it only when documented performance supports the change. | Interval must be risk- and history-based |