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The Chiller That Lives in a Vacuum

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The Chiller That Lives in a Vacuum

A 1998 400-ton centrifugal chiller, R-123, 900 lb charge, serves a hospital. Logs show the purge unit running 16–18 hours a day (normal is under 2), the purge counter climbing steadily, and condenser approach temperature rising from 2°F to 9°F over three months. With the machine off overnight, the evaporator pressure drifts from its normal 26 in. Hg vacuum (about 40°F saturation) to roughly 18 in. Hg vacuum. The maintenance supervisor proposes three things: (1) raise the machine to 12 psig with a nitrogen bottle to "find the leak fast," (2) charge liquid R-123 into the evaporator to "get the pressure up," and (3) if that fails, pull a deeper vacuum on the running machine to boil the moisture out. The machine's rupture disc is stamped 15 psig.

1. What is actually happening inside this machine, and how does that direct the leak search?

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The machine is pulling air and water in, not pushing refrigerant out. A low-pressure R-123 chiller runs below atmospheric pressure on the low side (about 26 in. Hg vacuum at 40°F saturation, roughly 1.9 psia). Any leak below atmospheric is an ingress path: air and moisture come in, refrigerant does not go out. That single fact explains every symptom:

  • Non-condensables collect in the condenser, raising the approach temperature from 2°F to 9°F.
  • The purge unit runs almost continuously because it is the only thing removing the air; its climbing counter is the diagnostic signal, not the fault.
  • The machine cannot hold vacuum when off - drifting from 26 to 18 in. Hg vacuum overnight is a large, fast in-leak.

Where to look. The low-side boundary: evaporator tube sheets and water-box gaskets, the rupture disc and its flange, the charging valve, the purge unit's own seals and piping, and the compressor shaft seal. The high-side (condenser) components at 100+ psig are not the likely source of an ingress leak - pressurizing the whole machine to chase a high-side leak would miss the point.

Detection method. Use an electronic detector suitable for R-123, or pressure the isolated section to a few psig with dry nitrogen and use soap solution. R-123 is a B1 refrigerant (higher toxicity, 50 ppm acceptable exposure limit); ventilate the machine room and monitor while working.

2. Critique the supervisor's 12 psig nitrogen pressurization plan.

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It is a defensible idea executed dangerously. A nitrogen pressure test is the right tool for a machine that normally sits in a vacuum, but three specifics make this plan unsafe:

  1. The margin is 3 psi. The rupture disc is stamped 15 psig. A regulator that creeps, a bottle warming in the sun, or a slug of liquid in a section can lift the disc and dump 900 lb of R-123 into a hospital machine room. Test at the lowest pressure that will reveal the leak - a few psig - isolate sections with valves where possible, use a nitrogen regulator with a relief device downstream, and watch the gauge continuously.
  2. Nitrogen only. Never use oxygen or compressed air. Oil plus oxygen under pressure is a fire/explosion hazard, and shop air supplies exactly the moisture the machine is already fighting.
  3. Never use the chiller's own compressor to build pressure. It is not a test compressor, and running it against a pressurized, non-condensable-filled circuit risks damage.

Also note the sequence problem: the machine still contains R-123. You cannot pressure-test a charged machine meaningfully, and you must not open it to atmosphere with refrigerant in it. Recover first to 25 mm Hg absolute with low-pressure (Type III) equipment, then leak-test, then repair.

3. Evaluate the liquid-charging proposal and the "deeper vacuum on a running machine" idea.

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Liquid into the evaporator: no. The evaporator is full of water at about 40°F. Dumping liquid R-123 into it flashes and can chill the water below freezing; a split tube then puts water into the refrigerant circuit and turns gasket work into a full rebuild. Charge R-123 as a vapor into the evaporator or suction side, with the chilled-water pump running, weighing the charge or following the manufacturer's charging chart. Verify the result with the machine's normal indicators, not by watching the low-side gauge climb.

Deeper vacuum on a running machine: impossible and harmful. You cannot evacuate a vessel that contains refrigerant - the pump would simply pull refrigerant out of the machine. Pulling below the manufacturer's specified limit can also damage motor windings and overload the purge. Moisture is removed by:

  • recovering to 25 mm Hg absolute with low-pressure recovery equipment,
  • replacing the dehydrator/filter-driers (moisture in an R-123 machine forms acids that attack the windings - the dehydrator is a maintenance item, not a decoration),
  • evacuating with a vacuum pump and a micron gauge, then performing a standing vacuum test before recharging.

The purge unit should be serviced and its efficiency verified, but it is a symptom-treater here; the leak is the problem.