| 1. Compact 2-Valve Block-and-Bleed | Isolates the process and vents the gauge side for safe removal or calibration. | Commonly rated from approximately 4,000 to 6,000 psi (276 to 414 bar), depending on design. | 316 stainless steel; carbon steel and alloy options are also available. | Process inlet, gauge outlet, and vent typically use NPT, BSP, or tube fittings. | General pressure measurement on transmitters, gauges, and instrument panels. | Small footprint, simple operation, and lower installation cost. | It does not provide a separate equalizing function for differential-pressure service. |
| 2. 3-Valve Equalizing Manifold | Provides isolation, equalization, and venting through three independent valves. | Commonly available around 3,000 to 6,000 psi (207 to 414 bar). | 316 or 316L stainless steel is widely used; PTFE or graphite packing may be selected. | Often supplied with female NPT, BSP, or compression-tube connections. | Single-gauge pressure monitoring where controlled equalization is required. | Allows safer zero checks and controlled pressure balancing. | More complex and larger than a basic 2-valve design. |
| 3. High-Pressure Needle-Valve Manifold | Uses a fine-thread needle valve for gradual isolation and precise throttling. | Many standard designs are rated to approximately 6,000 psi (414 bar); higher ratings require product-specific verification. | 316 stainless steel body and stem; metal-to-metal or soft-seat sealing options. | High-pressure NPT, BSP, tube, or cone-and-thread connections. | Hydraulic, gas, test, and laboratory systems operating at elevated pressure. | Excellent control of pressure release and reduced risk of hydraulic shock. | Slower to operate than a quarter-turn ball valve. |
| 4. Compact Ball-Valve Manifold | Provides rapid on/off isolation with a quarter-turn handle. | Typically selected for systems from vacuum service to approximately 6,000 psi (414 bar), subject to seat and temperature limits. | 316 stainless steel with PTFE, PEEK, or other application-specific seat materials. | NPT, BSP, tube, flange, and gauge-thread configurations are common. | Skid packages, utility lines, and applications requiring frequent isolation. | Fast operation and low pressure drop when fully open. | Rapid opening may cause pressure surges; it is less suitable for fine throttling. |
| 5. Sour-Service Single-Gauge Manifold | Provides isolation and venting while using materials selected for hydrogen sulfide exposure. | Commonly offered in pressure classes up to approximately 6,000 psi (414 bar), depending on the specification. | NACE-compliant or suitably hardness-controlled stainless steel; seal compatibility must be confirmed. | NPT, BSP, tubing, and flanged connections may be specified for process compatibility. | Oil, gas, petrochemical, and other sour-gas environments. | Improved resistance to sulfide stress cracking when correctly specified. | Material compliance, hardness, and documentation can increase cost and lead time. |
| 6. Low-Temperature Instrument Manifold | Isolates and vents a pressure gauge in cold ambient or cryogenic-adjacent service. | Pressure rating varies widely; common instrument versions fall within approximately 3,000 to 6,000 psi (207 to 414 bar). | 316L stainless steel is common; low-temperature seal and packing grades are essential. | NPT, BSP, tube, or welded connections, selected according to temperature and fluid service. | Refrigeration, LNG-related equipment, cold-weather installations, and gas service. | Maintains sealing performance over a broader temperature range. | Standard elastomers may harden or leak at low temperatures. |
| 7. High-Temperature Instrument Manifold | Provides gauge isolation and venting with packing and seals rated for elevated temperature. | Often rated from approximately 3,000 to 6,000 psi (207 to 414 bar), with pressure derating at high temperature. | 316 stainless steel with graphite, PTFE, PEEK, or other temperature-rated sealing materials. | Threaded or tube connections are common; welded ends may be used for severe service. | Steam, refining, process heating, and high-temperature industrial systems. | Better sealing reliability when temperature limits are properly engineered. | Maximum pressure and temperature must be checked together, not separately. |