
Chiller refrigerant pressure gauges are not interchangeable with standard industrial gauges. Each refrigerant circuit — high-side discharge, low-side suction, and maintenance vacuum — demands a different pressure range, Bourdon tube material, and connection standard. This guide covers gauge selection for R-22, R-134a, R-410A, R-407C, and CO2 (R-744) chiller systems, with decision points for range, accuracy class, and wetted materials.
Chiller refrigerant pressure gauges must match the saturation curve of each refrigerant. The table below gives the typical high-side and low-side pressures at common operating conditions:
| Refrigerant | High-side (condensing, 45°C) | Low-side (evaporating, 5°C) | Recommended gauge range |
|---|---|---|---|
| R-22 | ~17 bar (246 psi) | ~5.8 bar (84 psi) | High: 0–25 bar | Low: 0–10 bar or compound |
| R-134a | ~11.6 bar (168 psi) | ~3.5 bar (51 psi) | High: 0–16 bar | Low: compound –1 to 10 bar |
| R-410A | ~27.3 bar (396 psi) | ~9.4 bar (136 psi) | High: 0–40 bar | Low: 0–16 bar or compound |
| R-407C | ~17.5-19.7 bar (254-286 psi) | ~5.5-6.7 bar (80-97 psi) | High: 0–25 bar | Low: 0–10 bar |
| CO2 (R-744) | Up to 130 bar (1885 psi) | ~39.7 bar (576 psi) | High: 0–160 bar SS | Low: 0–60 bar SS |
A gauge sized at 130–150% of maximum operating pressure gives the best accuracy across normal working range while protecting the Bourdon tube from pressure spikes.
Read the table as absolute saturation pressure. A gauge on the machine reads roughly 1 bar (14.5 psi) less, because it measures against atmospheric pressure. R-407C is a zeotropic blend with temperature glide, so its saturation pressure is a bubble-point/dew-point band rather than a single value — the discharge gauge sits nearer the bubble point and the suction gauge nearer the dew point. Values calculated from reference equations of state; confirm against the chiller manufacturer's own P–T data before you set alarm points.
The high-pressure side of a chiller refrigerant circuit is where the compressor discharges hot gas into the condenser. Key selection criteria:
The chiller refrigerant low pressure gauge monitors the evaporator side where refrigerant boils at low temperature and pressure. Sub-atmospheric pressures occur during pump-down and commissioning:
For CO2 systems the low-side operating pressure at +5°C evaporating is already ~27 bar, so a low-side gauge rated to at least 40 bar is required — a standard HVAC compound gauge is completely undersized.
CO2 refrigeration operates at pressures 5–8× higher than HFCs. A standard HVAC manifold gauge set is dangerous on a CO2 chiller. Requirements:
Manogauge supplies stainless steel CO2 refrigerant pressure gauges in 0–100, 0–160, and 0–250 bar ranges, with ATEX option for ammonia–CO2 cascade systems.
Get CO2 Pressure Gauge QuoteOur engineers respond within 24 hours→Every pressure reading on a chiller is really a temperature reading. In the condenser and the evaporator the refrigerant is saturated — liquid and vapour coexist — so pressure and temperature are locked together by the saturation curve. That is why a technician can hold a surface thermometer against the suction line and predict what the gauge should show, and why a gauge that disagrees with the temperature is telling you something is wrong with the charge, the airflow or the water flow.
Saturation pressure in bar absolute:
| Refrigerant | -10 °C | 0 °C | +5 °C | +20 °C | +35 °C | +45 °C | +55 °C |
|---|---|---|---|---|---|---|---|
| R-22 | 3.55 | 4.98 | 5.84 | 9.10 | 13.55 | 17.29 | 21.75 |
| R-134a | 2.01 | 2.93 | 3.50 | 5.72 | 8.87 | 11.60 | 14.92 |
| R-410A | 5.74 | 8.00 | 9.35 | 14.45 | 21.42 | 27.30 | 34.36 |
| R-407C | 3.20-4.05 | 4.61-5.68 | 5.47-6.66 | 8.80-10.38 | 13.49-15.45 | 17.53-19.72 | 22.45-24.81 |
| CO2 (R-744) | 26.49 | 34.85 | 39.69 | 57.29 | - | - | - |
R-407C is shown as a dew-point to bubble-point band because of its temperature glide. CO2 has a critical point at 31.0 °C and 73.8 bar absolute, so above roughly 31 °C there is no saturation pressure at all — the high side runs transcritical and pressure is set by the gas cooler control, not by a P–T table. That is exactly why a transcritical CO2 high-side gauge must be sized on the control pressure and relief setting rather than on a condensing temperature.
Three practical uses of the P–T relationship at the gauge: convert suction pressure to saturated suction temperature and subtract it from the measured suction line temperature to get superheat; convert discharge pressure to saturated condensing temperature and compare with the leaving condenser water or air temperature to judge fouling; and, on a machine that has been off long enough to equalise, compare the standing pressure with the P–T value at room temperature to screen for non-condensables or a lost charge. See dial size selection for the readability side of this.

Standing pressure is what the gauges read after the machine has been off long enough for refrigerant and metal to reach the same temperature. On a healthy, correctly charged system both sides settle at the saturation pressure for that refrigerant at the measured ambient or shell temperature, so the standing reading is a free diagnostic: look up the temperature in the P–T table above and compare.
Pressure testing is a different job and needs a different gauge. Strength and tightness test pressures come from the applicable safety standard — EN 378 in Europe, ASHRAE 15 in North America — together with the equipment nameplate PS/MAWP; they are not a rule of thumb and must never be improvised. Practical gauge requirements for the test itself:
Evacuation after a successful pressure test is a vacuum measurement, not a pressure measurement — see the torr/micron discussion in the low-side section above. Related reading: overpressure protection and pressure gauge failure modes.
When placing an RFQ for chiller refrigerant pressure gauges, provide these parameters to avoid back-and-forth clarification:
Manogauge OEM chiller refrigerant pressure gauges are available as private-label assemblies for HVAC equipment manufacturers. Standard lead times are 15–25 days for OEM volumes, with express 7-day service for certified stainless steel CO2 gauges.
Related guides: A2L R-454B refrigerant pressure gauge selection and ammonia refrigeration pressure monitoring cover adjacent refrigerant gauge specifications.
Send Chiller Gauge RFQOur engineers respond within 24 hours→High-side, low-side and service gauge RFQs for HVAC/R and chiller systems.
Liquid-filled pressure gauge supplierUse for compressor vibration, pulsation and machine-room service panels.
CO2 transcritical refrigeration pressure gauge selection for R744 racks: high-side pressure, flash tank and suction points, materials and safety cases.
A2L R-454B refrigerant pressure gauge selection for HVAC service: manifold gauge use, PT chart checks, service ports, gauge range and safe workflow.
Vacuum pressure gauge selection: gauge, vacuum, compound and absolute references, the right sensing element per vacuum level, and where a dial stops working.
Why a steam pressure gauge needs a siphon: how the condensate barrier protects the Bourdon tube, pigtail vs coil vs U-type, filling and range checks.
Solid front pressure gauge selection for high pressure, gas and steam service: safety case design, blow-out back, ASME B40.100 and EN 837-1 S3 patterns.
No. Standard HVAC brass manifold gauges are rated to approximately 45 bar maximum. CO2 (R-744) chiller high-side pressures can reach 130 bar or above in transcritical operation. Using an undersized gauge is a safety hazard. Always use stainless steel gauges rated to at least 160 bar, designed specifically for CO2 refrigerant service.
A low-pressure chiller gauge measures refrigerant suction-side pressure — typically 0 to 10 or 16 bar — during normal operation. A torr vacuum gauge is used during system evacuation before refrigerant charging and must resolve to 50 microns (0.05 Torr) or better to confirm moisture removal. Bourdon tube pressure gauges cannot resolve vacuum at this level; electronic thermocouple or Pirani gauges are required for torr-range measurements.
For R-410A: high-side gauge 0–60 bar, Class 2.5 accuracy minimum (Class 1.6 for panel instruments), brass or stainless steel, 1/4" SAE flare or 1/4" NPT connection. Low-side: compound gauge –1 to +16 bar or a 0–16 bar gauge if the suction does not go below atmospheric. Glycerine filling is recommended if the compressor creates pulsation.
Annual calibration is standard practice for chiller machine-room gauges used in charge verification or fault diagnosis. Glycerin-filled gauges typically maintain accuracy longer than dry gauges because fill dampens compressor micro-vibration. Gauges used only for visual monitoring during normal operation may follow an extended 2–3 year cycle if plant risk assessment permits.
100 mm nominal dial is the minimum for readability at arm's length in a plant room. EN 837-1 accuracy class 1.6 suits routine monitoring; specify class 1.0 for gauges used during commissioning, leak checks or refrigerant charge verification. For low-side gauges reading below 5 bar, verify that the scale graduation spacing is adequate — a 0–10 bar range on a 100 mm dial reads more clearly than a 0–16 bar range at the same nominal size.
With the machine off long enough for refrigerant and metal to equalise, both sides settle at the saturation pressure of that refrigerant at the measured ambient or shell temperature. For R-134a at 20 °C that is about 5.7 bar absolute (roughly 4.7 bar on the gauge); for R-410A about 14.5 bar absolute (roughly 13.5 bar on the gauge). A standing pressure clearly above the P–T value usually means non-condensables such as air in the circuit; clearly below usually means an undercharge or a leak. Give the machine enough off time for temperatures to actually settle before you judge the reading.
Strength and tightness test pressures come from the applicable safety standard — EN 378 in Europe, ASHRAE 15 in North America — together with the equipment nameplate PS/MAWP, not from a rule of thumb. Test with dry nitrogen, never oxygen. Use a dedicated test gauge whose full scale is above the test pressure but close enough that the pointer sits in the upper half of the dial, and specify accuracy class 1.0 or 1.6: a class 2.5 service gauge cannot resolve the small decay that proves a slow leak. Correct for ambient temperature over the hold period, because nitrogen in a fixed volume changes pressure roughly 0.3–0.4% per kelvin. Never read the test pressure on the manifold's low-side compound gauge.