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Helium Leak Testing Equipment
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Vacuum Chamber Helium Leak Testing Machine 1.0E-9 Mbar.L/S Two Chambers For Liquid Cooling Cold Plates

Vacuum Chamber Helium Leak Testing Machine 1.0E-9 Mbar.L/S Two Chambers For Liquid Cooling Cold Plates

Brand Name: HongCe
MOQ: 1 Set
Payment Terms: T/T, L/C at sight
Supply Ability: 6 Sets per Month
Detail Information
Place of Origin:
Guangdong, China
Certification:
CE, ISO 9001:2015
Machine Configuration:
Two Chambers, Phase-shifted, Pneumatic Lid
Chamber Internal Size:
700 X 600 X 500 Mm Each, Customisable
Minimum Detectable Leak:
1.0E-9 Mbar.L/s
Gross Leak Stage:
0.1 - 3.0 MPa With Pressure Hold
Cycle Time:
60 S Per Plate, 45 S On Small Plates
Throughput:
About 100 Plates Per Hour
Helium Recovery Rate:
>= 95%
Control System:
PLC With 15-inch HMI, 100 Recipes
Traceability:
Barcode, Result Log, MES Via Ethernet
Power Supply:
AC 380 V, 3-phase, 18 KW
Weight:
2800 Kg
Packaging Details:
Skid-mounted frame with rust preventive film, chamber sealed with desiccant, sea-worthy plywood enclosure
Highlight:

Dual Chamber Cold Plate Testing

,

Helium Recovery Vacuum Leak Detection

,

Liquid Cooling Plate Airtightness Test

Product Description
Detectable band1.0E-9 mbar·L/s
Cycle60 s per plate, 45 s on small parts
Chambers2, phase-shifted
Helium recovery≥95%

A cold plate that weeps does not fail in your factory. It fails in a rack, a year later, when the coolant has been quietly topping itself up and the leak finally reaches something expensive. This two-chamber helium system is built to catch that defect at the line, at a takt the line can actually hold.

This machine is the right purchase if

  • You build liquid cooling plates, cold plates or liquid-cooled housings for servers, power electronics or vehicles.
  • Your seams are friction stir welded, vacuum brazed or gasketed — joints that cannot be repaired after assembly.
  • Your customer measures coolant loss or IP rating, not just burst pressure.
  • You need 100% inspection with a record attached to every serial number.

Look elsewhere if

  • Your annual volume is a few hundred plates and a sample test is enough.
  • The plate is fully serviceable and a leak can be fixed in the field.
  • Your acceptance criterion is a hydrostatic burst test — that is a different machine, and we build those too.

What actually fails on a cold plate

Almost never a hole you could see. The failures we are called in to explain come from the joining process, and they share one property: they are small enough to pass a water test and large enough to matter over a service life.

  • Friction stir weld defects. A worm hole or a lack of penetration along the weld toe. The joint looks continuous, the water test holds, and the leak opens once the plate has been through a few hundred thermal cycles.
  • Braze voids in the channel joint. Same story in a vacuum-brazed plate: a void that is bridged by a thin film of filler and fails in fatigue.
  • Port threads cut too deep. The fitting bottoms out on the thread instead of the seal face, and it weeps only under pressure and at temperature.
  • Header and manifold welds. The heat cycle leaves a crack that starts at the toe and grows.
  • Handling damage. A plate that has been dropped often looks perfect and leaks at the port.

Why water and air tests are not enough

A hydrostatic test proves the plate will not burst today. It does not prove it will stay sealed for eight years, because the defects that cause returns are two to four orders of magnitude below what a water test resolves.

Air decay is cleaner and faster, but a cold plate has the worst possible geometry for it: a small internal volume, a large metal mass that fights temperature stability, and a criterion that is usually tighter than air can resolve inside a takt. You end up either accepting a coarse limit or waiting three minutes per part.

Helium inside the plate, vacuum outside it, and a mass spectrometer reading the rise. The plate is never exposed to internal vacuum, so a thin plate stack is not deformed by the test itself — which is a real risk on a 1 mm channel wall.

A number worth remembering

Leak rates confuse people because the units look academic. One useful conversion: 1×10-6 mbar·L/s is roughly 0.6 mL per minute of gas at atmospheric pressure — about 300 litres a year. For a coolant circuit that is a visible loss, not a theoretical one.

Which is why the acceptance criterion deserves a proper conversation. A plate specified at 1×10-5 mbar·L/s is allowed to lose litres of coolant over a service life. A plate at 1×10-7 is not. Both are "leak tested"; only one of them will keep a data hall dry.

Design choices and why we made them

Gross stage first, fine stage second

Helium enters at up to 3.0 MPa and the pressure is held. A plate with a bridged weld is rejected in seconds, before the analyser is asked to work. This is what turns a three-minute test into a one-minute test.

Two chambers, out of phase

While one chamber measures, the other is unloaded and reloaded. One operator, about a hundred plates an hour. A single chamber with the same sensitivity needs a second person to reach that output.

Recovery sized for a high cycle count

A hundred plates an hour, two shifts a day, is a lot of helium down the vent if you do not recover it. The loop is integrated with purification after the buffer, so what goes back into the next plate is still within specification.

A drying option, because plates arrive wet

If a plate has been through a water circuit, that moisture outgasses under vacuum and reads as a leak. We can add a dry-air purge step to the recipe, or you can test before the water circuit is filled — both work, guessing does not.

How a cycle runs

  • Load and clamp — plate into the chamber, coolant ports connected, pneumatic seal on the lid, barcode scan.
  • Evacuate — roots and rotary pump set pull the chamber down; the recipe waits for a stable base pressure.
  • Gross stage — helium charge to the recipe pressure and hold; a pressure drop ends the cycle immediately.
  • Fine stage — analyser integrates the chamber signal and converts it to a leak rate against the limit.
  • Recover and release — helium pulled back, chamber vented, plate released with a verdict and a stored record.

Technical parameters

ItemSpecification
Machine configurationTwo chambers, phase-shifted, pneumatic lid, skid-mounted
Chamber internal size700 × 600 × 500 mm each, customisable
Minimum detectable leak1.0×10-9 mbar·L/s
Gross leak stage0.1 – 3.0 MPa helium charge with pressure hold
Cycle time60 s per plate typical; 45 s on small plates
ThroughputAbout 100 plates per hour with one operator
Helium recovery≥95% with recovery and purification loop
Vacuum systemRoots pump plus rotary vane pump per chamber, oil filtration
ControlPLC with 15-inch HMI, 100 recipes, multi-level access
TraceabilityBarcode scan, per-plate result log, MES upload over Ethernet
CalibrationAutomatic sequence with calibrated leak, 12-month interval
Power supplyAC 380 V, 3-phase, 50/60 Hz, 18 kW
Compressed air0.6 MPa dry, oil-free, 300 L/min
WeightAbout 2800 kg

What it finds

Test itemTypical defectWhy the factory test misses it
Friction stir weld seamWorm holes, lack of penetration at the toeHolds at low pressure, opens under cycling
Brazed channel jointBraze voids, flux inclusionsSmall enough to pass a water test
Tube-to-plate port jointRelaxation after thermal cyclingOnly leaks when warm and pressurised
Port threads and O-ring groovesThread cut too deep, damaged grooveSeal face never contacts
Channel wallMachining porosity, thin wall at the bendBelow air-test resolution
Header and manifold weldsCracks from the weld heat cycleInvisible, grows in service
Plate after proof pressureDamage caused by the pressure testNobody re-tests after proof

Setting the limit, and proving the machine can hold it

  • Work backwards from coolant loss. Use the conversion above, the coolant volume and the acceptable annual top-up, and derive the rate. Most server cold plates land between 1×10-6 and 1×10-7 mbar·L/s.
  • Run ten good plates and ten with a calibrated leak. If the two populations are separated by a factor of three or better, the test is sound. If they overlap, lengthen the test rather than tightening the limit.
  • Repeat after a process change. A new weld program or a new brazing cycle changes the defect population, and the limit should be revalidated, not inherited.
  • Document the method with the limit. Charge pressure, dwell, chamber size, ambient band. Auditors ask for it, and so will your customer's quality engineer.
Plates that have been water tested will read high until they dry. If your process fills the coolant circuit before the leak test, tell us at the enquiry stage — we size the pump set and the purge step for that case, and it changes the cycle time.

Compared with the alternatives

MethodDetectable bandCycleEffect on the plateWhere it belongs
Two-chamber helium, this machine1×10-9 mbar·L/s45–60 sDry, external vacuum only100% final inspection
Air pressure decayAbout 1×10-3 mbar·L/s1–5 minDryGross defects only
Hydrostatic proof testBurst strength onlyMinutesWets the plateSafety verification, not leak control
Helium sniffer spray1×10-7 mbar·L/s2–10 minDryLocating failures at the rework bench

The comparison that usually decides the purchase is not with the alternatives but with the cost of a field failure: a rack pull, a coolant cleanup, a customer visit and a reputational hit that no test machine budget can absorb. Once a customer has had one, 100% inspection stops being a cost argument.

Delivery, installation and the first month

  • Factory acceptance test on your plates before shipment, with video and calibration record.
  • Fixture and port connector concept agreed against your drawing before fabrication.
  • On-site commissioning: fixture prove-out, leak-rate correlation against a calibrated leak, operator training.
  • Repeatability study on good plates and a calibrated-leak plate, signed off with your quality engineer.
  • Recipe per plate family, selected by barcode, with the drawings handed over.
  • 24-month warranty on mechanics, pneumatics and control; pumps per manufacturer terms.
  • Spares in Guangzhou: lid seals, port connector seals, helium valves, pump service kits — 48-hour dispatch.
  • Annual calibration with traceable certificate and remote support for recipe tuning.

Frequently asked questions

Why not just pressure test with water and be done?

Because a hydrostatic test answers a different question. It proves the plate will not burst at 1.5 times working pressure; it says nothing about a 10-6 mbar·L/s weep that will empty a coolant loop over a service life. And it leaves water in the channels, which then interferes with any sensitive test you run afterwards.

How much helium does each plate consume?

With recovery running, a few litres per shift for small plates. Losses come from lid sealing and venting rather than from the plate volume. We quote consumption per 1000 plates based on your chamber size and cycle count, because the per-part number is what your cost model needs.

What leak rate should we specify?

Start from acceptable coolant loss over the service life, then convert. For server cold plates our customers typically work between 1×10-6 and 1×10-7 mbar·L/s. Bring the coolant volume and the loss target and we will help you do the arithmetic in the enquiry.

Can we test a different plate size later?

Yes, within the chamber envelope. Below that, a new fixture and a new recipe is normally all it takes. Keep the fixture drawings and a second plate family is a few days of work, not a second machine.

The plate arrives wet from the water test. Is that a problem?

It is if you ignore it. Moisture outgasses under vacuum and reads as a leak. Either test before the water circuit is filled, or add a dry-air purge step — we build the recipe for the case you actually have.

What happens to a rejected plate?

The chamber test tells you it leaks; finding where is a probe job. A sniffer sweep along the weld and around the ports usually localises it in a couple of minutes, which is enough to decide between rework and scrap.

How stable does the shop temperature need to be?

Less critical than with air testing, because the measurement is on helium rather than on a pressure difference. Avoid a station in direct sun or next to a furnace door, and the compensation has little to do.

Lead time?

Around 90 working days for a two-chamber system with fixtures. The chamber, recover loop and fixture are all built to order; standard sub-assemblies are held in stock to keep that date realistic.

About Guangzhou Hejin Automation Control Technology

Since 2003 we have built leak detection and electrical test equipment in Guangzhou, with 50–100 employees and around half of our production exported. Our engineers commission chamber systems, tracer gas hoods and air decay testers on the same floor, so the recommendation for a cold plate comes from test data rather than from a catalogue.

Every system is assembled, pump-down tested, calibrated and recorded under its serial number before it leaves us. When a question comes up three years later, the original test data is still on file.

Send a cold plate drawing, the coolant, the working pressure and the leak rate target. We will propose a chamber size, a fixture concept and a cycle time, and quote the helium consumption per 1000 plates so the running cost is comparable with the alternatives.