| Primary Function | Use a two-valve single gauge manifold for pressure indication, instrument isolation, and controlled depressurization. | One process isolation valve plus one vent or bleed valve connected to a single pressure gauge. | This configuration allows the gauge to be isolated for inspection or replacement without shutting down the entire process, where the installation design permits it. |
| Pressure Range | Select a gauge and manifold whose maximum allowable working pressure exceeds the normal and abnormal pressure conditions of the system. | Common gauge scales include 0–1.6, 0–2.5, 0–4, 0–6, 0–10, 0–16, 0–25, and 0–40 bar; equivalent psi scales are also widely used. | For improved readability and reduced mechanical stress, normal operating pressure is commonly kept near the middle portion of the gauge scale rather than at the upper limit. |
| Pressure Class Verification | Confirm the pressure rating of the complete assembly, including the body, valves, fittings, tubing, seals, and gauge connection. | Do not treat a nominal connection size or thread type as a pressure rating. Ratings must be checked at the actual operating temperature. | The lowest-rated component determines the safe working limit of the assembled manifold system. |
| Process Temperature | Specify the minimum, normal, and maximum process and ambient temperatures. | Standard metallic manifolds are often used in ambient service around −20 °C to 80 °C, but the permitted range depends on the material, seal, gauge, and connection design. | Temperature can reduce seal performance, change material strength, and affect the pressure rating of the assembly. |
| Process Fluid Compatibility | Match all wetted materials with the process fluid, including the body, stem, seat, packing, gasket, and diaphragm or sensing element. | 316 or 316L stainless steel is widely selected for general industrial and many corrosive services. Nickel alloys or special materials may be required for highly aggressive media. | Material compatibility reduces corrosion, leakage, contamination, and premature failure. |
| Gas, Liquid, or Steam Service | Identify whether the manifold will handle gas, liquid, condensable vapor, steam, oxygen, or hazardous media. | Steam and hot vapor service may require a cooling leg, siphon, impulse line, or remote installation. Gas service may require leak-tight connections and controlled vent routing. | Fluid phase and temperature influence measurement accuracy, installation orientation, drainage, and operator safety. |
| Valve Arrangement | Use a straight-through block-and-bleed arrangement when one gauge requires isolation and venting. | A single gauge manifold normally has two functional valves: process isolation and vent or bleed. It does not provide transmitter equalization unless specifically designed for that purpose. | Choosing the correct valve arrangement prevents unnecessary complexity and avoids using a single gauge manifold for differential-pressure applications that require equalization. |
| Connection Type | Match the process and gauge connections to the piping specification and installation method. | Common options include NPT, BSPP, BSPT, tube compression connections, and flanged interfaces. Typical gauge ports include 1/4 or 1/2 nominal connections, subject to the design. | Correct thread form, size, sealing method, and engagement length are essential for mechanical integrity and leak prevention. |
| Seal and Packing Material | Select seals according to fluid chemistry, temperature, pressure, and emissions requirements. | Common choices include PTFE, graphite, elastomers, and metal seals. Oxygen, sour-gas, high-temperature, and vacuum services may require special cleaning or sealing specifications. | The wrong seal can swell, harden, permeate, decompose, or leak under service conditions. |
| Gauge Accuracy | Choose accuracy according to the monitoring, control, or safety function of the gauge. | Industrial gauges are commonly available with accuracy classes such as 0.5, 1.0, or 1.6 percent of span, depending on the gauge design and applicable standard. | Higher accuracy may be necessary for calibration, testing, or process control, while general indication may not require it. |
| Vibration and Pulsation | Assess pump pulsation, compressor vibration, water hammer, and pressure cycling before selecting the gauge and manifold. | Possible measures include a liquid-filled gauge, snubber, restrictor, pulsation dampener, remote mounting, or reinforced tubing arrangement. | Reducing pressure spikes and vibration improves gauge life, reading stability, and connection reliability. |
| Vent and Drain Direction | Orient the bleed outlet toward a safe collection point or a closed vent system. | For hazardous, toxic, flammable, or environmentally regulated media, use tubing or piping to route the discharge to an approved containment or recovery system. | A bleed valve must not discharge toward personnel, electrical equipment, walkways, or unprotected work areas. |
| Installation Orientation | Install the manifold and gauge in a position that supports readability, drainage, venting, and maintenance access. | Liquid lines are generally arranged to avoid unwanted gas pockets; gas lines are arranged to avoid liquid accumulation at the sensing point. Final orientation depends on the process and gauge design. | Correct orientation helps prevent measurement error, corrosion, freezing, and trapped pressure. |
| Applicable Standards | Specify the standards required by the project, industry, location, and pressure equipment regulations. | Relevant references may include ASME B40.100 for pressure gauges, ISO 5171 for pressure gauges, ASME B16.5 for applicable flanged interfaces, and ISO 15156/NACE MR0175 for selected sour-service materials. | Standards define requirements for materials, dimensions, testing, accuracy, and service suitability. The applicable edition and project specification should always be confirmed. |
| Testing and Documentation | Require pressure testing, leak testing, material traceability, and calibration documentation when the application demands it. | Typical records may include a hydrostatic or pneumatic test report, material certificate, gauge calibration certificate, and cleaning certificate for special services. | Documented verification supports commissioning, maintenance, audits, and safe replacement. |
| Safety and Maintenance | Provide a safe isolation and depressurization procedure before gauge removal or manifold maintenance. | Close the process isolation valve, verify zero pressure through the bleed path, and confirm that the vented fluid is safely contained before loosening any connection. | A closed isolation valve alone does not prove that the gauge connection is pressure-free. |
| When a Single Gauge Manifold Is Not Suitable | Use a different manifold configuration when the measurement requires more than simple gauge isolation and bleeding. | Differential-pressure transmitters generally require a three-valve or five-valve manifold. Multiple instruments may require separate isolation points or an engineered valve assembly. | Selecting a single gauge manifold for a multi-line or differential-pressure application can prevent proper equalization, calibration, and safe maintenance. |