8.5 Vacuum Systems, Pumps & Venturi Generators
Key Takeaways
- Vacuum is measured as pressure below atmospheric: a perfect vacuum is 0 kPa absolute, 101.3 kPa below atmosphere, or 29.92 in Hg of gauge vacuum at sea level.
- A vacuum cup can never develop more than about 101 kPa (14.7 psi) of holding pressure, so lifting capacity is set by cup area and the achievable vacuum level, with a safety factor applied.
- Venturi (ejector) vacuum generators have no moving parts and produce vacuum instantly from compressed air, but consume air continuously unless fitted with a vacuum switch and check valve.
- Oil-sealed rotary vane pumps reach much deeper vacuum than dry pumps but require gas ballast to purge condensable vapours from the oil.
- A vacuum system that will not pull down is diagnosed first by isolating and blanking sections to separate a leaking line or seal from a worn pump.
Task E-22 covers pneumatic and vacuum systems, 9 of the 135 exam questions. Millwrights service vacuum on packaging lines, plywood and veneer presses, dust collection, degassing systems, vacuum lifters and pick-and-place tooling.
Measuring Vacuum
Vacuum is not a separate quantity — it is pressure below atmospheric. The confusion comes from the three scales in common use:
| Scale | At atmosphere | At perfect vacuum |
|---|---|---|
| Absolute pressure | 101.3 kPa (14.7 psia), 760 torr | 0 |
| Gauge vacuum (in Hg) | 0 in Hg vacuum | 29.92 in Hg vacuum |
| Percentage of vacuum | 0% | 100% |
Worked conversion. A gauge reads 20 in Hg of vacuum at sea level. As a percentage that is 20 / 29.92 = 66.8%, and the absolute pressure remaining is (1 - 0.668) x 101.3 = 33.6 kPa absolute.
The hard ceiling: because vacuum works by removing pressure rather than adding it, the maximum differential available at sea level is only about 101 kPa (14.7 psi). There is no way to get more, and altitude reduces it further. Every vacuum-lifting calculation starts from that limit.
| Range | Absolute pressure | Typical equipment |
|---|---|---|
| Rough vacuum | 101 to 0.1 kPa | Rotary vane, liquid ring, claw, venturi — nearly all plant work |
| Medium vacuum | 0.1 kPa to 0.1 Pa | Roots blower boosters, oil diffusion |
| High vacuum | Below 0.1 Pa | Turbomolecular, cryogenic — laboratory and coating work |
Vacuum Pump Types
| Pump | Principle | Characteristics |
|---|---|---|
| Oil-sealed rotary vane | Vanes in an eccentric rotor, sealed and lubricated by oil | Deep vacuum (to about 0.1 Pa for two-stage), quiet; oil must be changed on schedule and mist eliminated at the exhaust |
| Dry rotary vane | Carbon vanes, no oil | Clean, no oil carryover; shallower vacuum, vanes are consumable |
| Liquid ring | A ring of liquid (usually water) thrown against the casing forms the sealing chambers | Tolerates wet, dirty and condensable gas streams; limited by the vapour pressure of the sealing liquid |
| Claw / screw (dry) | Non-contacting rotors | No oil, low maintenance, high efficiency; higher capital cost |
| Roots blower (booster) | Two-lobe rotors | Used as a booster on top of a backing pump to increase pumping speed |
| Venturi / ejector | Compressed air through a converging-diverging nozzle entrains air | No moving parts, instant response, compact, mountable at the tooling |
Gas ballast on an oil-sealed rotary vane pump admits a controlled bleed of atmospheric air into the compression stage so that condensable vapour — usually water — stays as vapour and is exhausted rather than condensing into the oil. Running a pump on a wet process without gas ballast turns the oil milky, destroys its sealing ability and ruins the pump. If oil looks milky, run the pump with ballast open and the intake blanked until it clears, then change the oil.
Venturi Vacuum Generators
VENTURI VACUUM GENERATOR (EJECTOR)
compressed air ==> [ nozzle ]>>>>[ diffuser ] ==> exhaust (silencer)
||
|| entrained air
||
vacuum port <-- to cup / tooling
Compressed air accelerates through a nozzle, and the resulting low-pressure region draws air in through the vacuum port. Advantages: no moving parts, instant vacuum and instant release, tolerant of duty cycling, and mountable right at the tooling to minimize evacuation time.
The drawback is air consumption. A generator running continuously on an idle machine wastes large volumes of compressed air. Best practice is an air-saving circuit: a vacuum switch senses that the set vacuum level is reached, a non-return (check) valve holds the vacuum in the sealed volume, and the generator shuts off until the level decays. A blow-off pulse of positive air then releases the part instantly.
Vacuum Lifting
Vacuum cup capacity follows the same force-equals-pressure-times-area relationship as hydraulics, with the differential capped at atmospheric pressure.
Worked example. Four cups of 150 mm diameter operate at 70 kPa of vacuum.
That is the theoretical holding force. A vacuum lifter must then apply the manufacturer's and the regulation's safety factor — commonly at least 2:1 for horizontal lifting and higher for vertical or tilting handling — plus allowances for surface porosity, contamination, temperature and acceleration forces. Any vacuum lifting device used overhead requires a vacuum reservoir or a fail-safe backup and an audible low-vacuum alarm, so a loss of power or supply air does not drop the load.
Filtration, Moisture and Maintenance
- Inlet filtration is mandatory: any dust, fibre or liquid drawn into a vacuum pump will damage vanes, seals or rotors. Check and change inlet filters on a schedule and after any process upset.
- Exhaust mist filters on oil-sealed pumps capture oil aerosol and return it to the sump; a plugged exhaust filter causes high back-pressure, oil carryover and pump overheating.
- Moisture separators and knockout pots protect the pump from condensate.
- Oil condition on an oil-sealed pump: change on schedule and immediately whenever it turns dark, milky or carries an odour.
- Vacuum hose and tubing must be rated for vacuum — ordinary flexible tubing collapses. Reinforced hose or rigid tube is required.
- Leak-check with a vacuum decay test: isolate the system, record the vacuum, and time the rate of rise. A rapid rise means leakage; a slow rise means outgassing.
Troubleshooting
| Symptom | Probable causes |
|---|---|
| Will not pull down to setpoint | Leak in a line, fitting or seal; failed check valve; worn pump vanes; low or contaminated oil; plugged inlet filter |
| Pulls down slowly | Undersized pump or line, long small-bore tubing, restricted filter, large system volume |
| Vacuum decays quickly when the pump stops | Leaking check valve, porous or damaged cups, cracked tubing |
| Milky pump oil | Water vapour condensing in the pump — open the gas ballast and correct the moisture source |
| Overheating pump | Restricted exhaust filter, low oil, high ambient, running at deep vacuum continuously without cooling |
| Cups will not release the part | Blow-off circuit not functioning, or the check valve holding vacuum in the cup |
Diagnostic method: blank the pump inlet and measure the vacuum the pump alone can achieve. If it reaches specification at the inlet, the pump is good and the fault is in the system — then isolate and blank sections progressively to find the leak. If the blanked pump cannot reach specification, the pump itself needs service.
Safety: never place a hand or any body part over an open vacuum port or cup — a large cup at full vacuum can hold hard enough to cause serious injury. Vacuum vessels can implode: they must be rated for external pressure, and an atmospheric tank is never used as a vacuum receiver.
A vacuum lifter uses six cups of 200 mm diameter operating at 60 kPa of vacuum. What is the approximate theoretical holding force, and what governs the actual rated capacity?
An oil-sealed rotary vane vacuum pump serving a wet process has milky oil and can no longer reach its rated vacuum. What is the correct diagnosis and remedy?
A packaging machine uses venturi vacuum generators that run continuously, and the plant compressed air system is struggling to keep up. What is the appropriate corrective measure?