Pressure Testing Refrigeration Systems

Pressure Testing Refrigeration Systems - HVAC Know It All
Key Takeaways
  • Test Pressure Calculation: Use (1.25) × Maximum Operating Pressure (MOP) based on your refrigerant type and Saturated Condensing Temperature (SCT)
  • Nitrogen Selection: Always use food-grade nitrogen for testing – it’s dry, clean, and won’t contaminate your system
  • Small vs Large Systems: Systems under 3 tons refrigeration/5 tons AC don’t require TSSA inspection; larger systems need 24-hour tests with calibrated gauges
  • Safety First: Never hydrostatically test with water, always wear safety glasses, and ensure proper regulator matching for high-pressure bottles

Why Pressure Test?

When construction or repair of a refrigeration system is complete, it is standard procedure to perform a Pressure Test. Pressure Testing describes the practice of pneumatically testing the piping and components of the system by adding a test fluid until the desired test pressure is met.

The reason a Pressure Test is done is to ensure there are no leaks in the system before the vacuum is pulled and the refrigerant is charged. In this article, I’ll cover important practices for Pressure Testing as it applies to different sizes and types of refrigeration systems.

Two Different Analog Refrigeration Gauges

Best Practices & Considerations

The upper bounds of your test will be determined by the Maximum Operating Pressure of the refrigeration system you are testing. The two pieces of information you need to determine this are the Refrigerant Type for the system and the Saturated Condensing Temperature (SCT) the system is intended to operate at. (1.25) × (Max Operating Pressure (MOP)) is common practice for testing refrigeration systems, aligning with specifications from ASME (American Society of Mechanical Engineers), TSSA (Technical Standards and Safety Authority), and CSA (Canadian Standards Association).

ASME are American standards which are internationally accepted and specified, while TSSA and CSA standards are relative to my work area of Toronto, Canada. Refrigeration Systems in this area are constructed, repaired, and tested as per CSA B52 Mechanical Code, and have systems field inspected by TSSA when required. PSIG (Pounds Per Square Inch Gauge) is the commonly used pressure increment in this region, so these are the units I will use throughout the rest of this article.

> Note: The industry also uses kPa (kilopascal) (6.895kPa = 1 PSI), as well as Bar on CO2 systems due to their high pressures (14.5PSI = 1 Bar).

Nitrogen

The testing fluid most appropriate is Nitrogen (atomic number N7). Most of the air that we breathe is nitrogen – air’s composition can be seen below.

> Note: It is never advisable to hydrostatically test a refrigeration system using water.

An illustration of Dalton's law using the gasses of air at sea level (Source: Wikipedia)
An illustration of Dalton’s law using the gasses of air at sea level (Source: [Wikipedia](https://en.wikipedia.org/wiki/Dalton%27s_law#))

The industry uses “Food Grade” Nitrogen for Refrigeration System Pressure Testing: it is clean of contaminants and, most importantly, very low in moisture content.

> Note: Medical Grade Nitrogen goes a step further, being extremely dry.

Moving on to the format of Nitrogen and getting it into the system, the next image below is from Josef Gas and shows us the different nitrogen bottle sizes available on the market.

The bottle, or “Bulk Pack” (16 Nitrogen bottles tied together in parallel with a common outlet), is then connected to a Nitrogen Regulator. There are Standard Nitrogen Regulators and High Pressure Nitrogen Regulators.

Their difference is a max regulator inlet pressure (from the Nitrogen Bottle) of 4000PSIG or 6000PSIG (see image above). Respectively, they also have different Delivery Pressures available on the outlet side of the regulator (to the system), represented on their gauge.

These 2 classes of regulators have different thread patterns on them to avoid the possibility of connecting a Standard Regulator to a High Pressure Bottle (or Bulk Pack) where a failure would occur.

The differences in size of nitrogen bottles

Small Refrigeration Systems

Starting with Small Refrigeration Systems, we will categorize this as anything under “3 tons or less of refrigeration, or 5 tons or less of Air conditioning” – as per ORAC (Ontario Refrigeration & Air Conditioning, paragraph 3 of this webpage on brazing). It is stated here that a TSSA Inspection/Pressure Test Witness is not required below these system capacities.

For Small Systems, consider the piping and components all being in a local area. This would include:

  • Roof Top Units
  • Split systems of any type: Furnace, Ductless Split, Window Shaker (so long as they do not have very long piping runs)
  • Appliances (Fridges/Freezers of any type)
  • Self Contained Units (Absorption Systems, Heat Recovery Systems, Heat Pumps)
  • Small Critically Charged Freezers and Coolers

> Note: Chillers straddle between a Small and Large System, as their Refrigeration System is contained within one area but is however large capacity, well above the ORAC tonnages stated.

Pressure Testing a Small System is usually a straightforward, simple procedure (see image below of a Ductless Split). If all system components and piping can be accessed in one or two areas, it simplifies the process/time taken of leak checking and completing a Pressure Test. Not having to schedule TSSA for inspection(s) also makes the install or system repair easier to plan and schedule.

A popular residential air conditioning refrigerant is R134a, and a common operating point for it is 120°F Saturated Condensing Temperature (SCT). The SCT is the basis of the highest temperature and pressure realized in a system. To find the pressure related to this Saturated Temperature, utilize a Pressure Temperature Chart (such as Bitzer Refrigerant Ruler):

  1. Take your SCT of 120°F to the Pressure Temperature Chart
  2. Find the “Saturated Condensing Pressure” of 171.1PSIG
  3. Following the previously mentioned equation: (1.25) × (MOP), we get (1.25) × (171.1PSIG) = 213.875PSIG. Round this to 214PSIG

So, 214PSIG is the max pressure we can achieve during testing. This is commonly rounded up to 225PSIG or 250PSIG for this refrigerant, as this is still well below max pressure ratings for most components. Be wary of exceeding pressure ratings of low side components however, such as a Low Pressure Cut-Out (LPCO). If low side components have lower pressure ratings than the intended max test pressure, it may be necessary to isolate the high side from the low side of the system and run two separate tests.

Test Plan for a Small System

For a system of this size, here is a plan to follow for Pressure Testing. This example is for a system which is “Flat” (empty / 0PSIG). We will use 250PSIG as our Final Test Pressure.

  • Ensure all system valves are open. Ensure safety glasses are worn.
  • Add nitrogen to achieve 50% of the Final Test Pressure: 125PSIG. This can be done by connecting the nitrogen bottle to a regulator and attaching the regulator to a refrigeration manifold which is connected to the system. Alternatively, the nitrogen bottle/regulator can be connected directly to the system (with an isolation valve in between), and a pressure gauge (preferably digital, for accuracy) attached directly to the system.
  • Quickly check the indoor unit/piping by listening (you can hear leaks at this pressure if the work area is quiet), and soap test using a Non-Corrosive Soap such as Big Blu. Ensure to soap more common leak points e.g., schrader valves/caps and flare connections. When replacing refrigerant hose seals, always check your manifold connections as well.
  • Quickly check the outdoor unit/piping with the same considerations as above. Ensure that all gauges/fittings/hoses that you are using for the pressure test are also soap tested.
  • If no leaks are found, you are ready to bump up to your final test pressure. Note: It is good practice to perform your first soap/leak check at this lower pressure to start. If nothing else, this would save Nitrogen in the case that you find a leak at the initial lower pressure (this would also save a considerable amount of time on a Large System).
  • Increase the system pressure to 250PSIG and start a timer for 1 hour. More time under test is preferred (more on this later), but 1 hour is common practice, as this allows you to begin Evacuation sooner. Note: Your “Vacuum Test” and “Decay Test” will add further certainty that your system is free from leaks.
  • Thoroughly check the indoor unit/piping by listening and soap testing everything: all piping and component connection points of any kind. An Inspection Mirror and Flashlight are a great help to be efficient and confident. You are looking to see if any soap is growing bubbles, i.e., a “Beard”. Very small leaks may need to be realized after the soap has sat on the leak for 15 minutes or more. As they say, no bubbles, no troubles.
  • Thoroughly check the outdoor unit with the same considerations as above. Again, ensure that all gauges/fittings/hoses that you are using for the pressure test are also soap tested.
  • If no leaks are found and the gauge has maintained 250PSIG, the pressure can now be blown off the system. Note: Release the pressure slowly whenever possible to avoid noise. If no one else is within earshot and you would like to blow the pressure off quicker: ensure the blow off point is stable (the hose is not loose) and wear appropriate hearing protection.
  • If evacuation is your next step, you want to time the end of your nitrogen blow down so that you have about 1-2PSIG remaining in your system and begin to pull the vacuum at this time. Note: If you blow a system down to 0PSIG, air will make its way back into the system through the open port. Just by adding and removing nitrogen, you have already removed a large volume of air from your system.
  • If you will not evacuate until later, blow down your system to 10-20PSIG. This is a common Safe Holding Charge Pressure, which keeps the system positive so that air does not enter the system.
An example of a Small System

Large Systems

Large Systems will be greater than 3 tons of refrigeration or 5 tons air conditioning. I will forego categorizing “Medium” Systems for conciseness. A Large System’s physical size/layout comes down to there being multiple locations which require inspection during the pressure test. There can be multiple people and multiple hours or days put into pressure testing a Large System.

The pressure testing may be done in multiple “Phases” during construction, as main portions of the systems are completed. Access to roofs, penthouses, valve stations, interstitial spaces, engine rooms, high ceiling hung evaporators, and other components may be required. Use of scissor lifts, boom lifts, and ladders are also common to access all points to be soap tested. Large System types include:

  • Supermarkets
  • Ice Rinks
  • Industrial Food Process Plants
  • Cold Storage Plants
  • Mining Refrigeration Systems
  • Commercial Heat Pumps and Heat Recovery Systems

Note that Large Homes also fall into this category if their system tonnage requires TSSA Inspection. Homes can have quite complex VRF Systems (Variable Refrigerant Flow) in them, tied into a home automation system much like a commercial Building Automation System (BAS).

An example of a Large System

TSSA Procedures for Large Systems

To ensure a system is leak free, a similar process is followed for a Small System or Large System. There are however many planning considerations which are unique to systems which require TSSA inspection. This is true in service/repair applications, but I will focus on new construction in this section for simplicity. Note: TSSA Inspections have extremely variable degrees of leniency or strictness, so I will list best practices below.

  • Material must be ordered, received, and inspected in accordance with required Material Specifications. Canadian Registration Numbers, Mill Test Reports, Data Reports, and Material Designations which match paperwork must be clearly stenciled/stamped onto piping and fittings from the manufacturers and circled or confirmed by the person who receives it on site. This is a required QC (Quality Control) Process.
  • TSSA will visit a very large project up to three times for a single “Phase” of the project. This includes a “Pre-Pipe Inspection,” another visit to confirm procedures are followed during construction, and a final visit for the TSSA Inspector (or person authorized on their behalf) to witness the Final Pressure Test.
  • These above considerations require planning ahead for material order and receival, as well as completion dates for significant sections of the project. Organization of material and its paperwork is paramount to being successful in a TSSA Inspection, on top of completing a successful Pressure Test.

When working with large systems that may have oil loss issues in screw compressors, pressure testing becomes even more critical to ensure system integrity before commissioning.

Pressure Testing Differences for Large Systems

There are some things which are unique to testing Large Systems compared to a Small System. These are both procedural and to ensure inspection requirements are met. Here are the points unique to Large Systems:

  • The Final Test Pressure must remain below 10% of any Relief Valve which will be part of the Pressure Test. Relief Valves may open 10% above or below their rated pressure. Another less preferred practice is removal of Relief Valves from the system until the Pressure Test is completed.
  • The test gauge must be calibrated (annually), and the Certificate of Calibration must be on-hand.
  • Nitrogen Bulk Packs may be used. A Bulk Pack is 16 Nitrogen bottles tied together in parallel with a common outlet. Each bottle still has its own handle, which allows the Refrigeration Mechanic to strategically open/close individual bottles, depending on his strategy to optimize pressure delivery to the

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Julian Finbow

313a Refrigeration Mechanic with main work experience in Industrial Refrigeration, and R&D. Course developer and teacher of HVAC/R and Plant Operation.

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