Process vacuum · Pump type, vapour handling and pump-down time
Start with the gas, not the pump. Water vapour, solvents and dust decide whether an oil-sealed pump survives or a dry screw pump is worth its price. Choose the type for the gas, then size the pumping speed for the pump-down time and the gas load at operating pressure.
Rough- and medium-vacuum pumps for drying, degassing, distillation, packaging, moulding and vacuum handling: oil-sealed rotary vane, dry screw, liquid ring and Roots combinations. Turbomolecular and other high-vacuum pumps are covered on the high-vacuum pump page.
01
Pfeiffer describes the rotary vane pump as oil-sealed: the oil lubricates, seals gaps and fills dead volume. It suits the low and medium vacuum ranges, ideally where the pumped medium does not condense at pump temperature; where substances attack the oil or condense despite gas ballast and accessories, a different backing pump should be selected. Two-stage versions reach lower ultimate pressures than single-stage ones. [1]
Dry screw pumps use two contactless counter-rotating screw rotors with no oil in the pumping chamber. Pfeiffer notes that water-cooled screw and multi-stage Roots pumps have been replacing oil-lubricated rotary vane pumps in the 100–600 m³/h class, and that its dry screw pumps suit chemical, dusty or condensate-producing processes; their effective pumping speed falls below about 1 hPa. [2]
Pfeiffer also notes that at high gas throughputs with gas ballast, oil mist is carried out of a rotary vane pump, which an oil mist filter can separate and return; filters and separators can protect against dust and some vapours within limits. [1]
Tell the supplier every gas and vapour in the stream, including solvents, water, acids and dust, their quantities and whether any are flammable. That list decides the pump type more than the target pressure does.
02
Leybold explains that vapour can only be compressed to its saturation pressure at pump temperature: water vapour in a pump at 70 °C condenses above 312 mbar, so it condenses before the exhaust valve opens. Gas ballast admits a defined quantity of air before compression so the valve opens first and the vapour leaves with the air. [4]
Leybold sets two conditions for pumping vapour: the pump must be at operating temperature and the gas ballast valve open; it advises running the pump for half an hour with the valve open first, which raises pump temperature by about 10 °C. [4]
Pfeiffer adds that without gas ballast a pump with an outlet below 100 °C cannot displace even small amounts of pure water vapour; condensate dissolves in the oil, raises the base pressure and can cause corrosion. Gas ballast slightly worsens the attainable base pressure, and water-vapour tolerance is quoted in hPa or mbar on the data sheet. [3]
03
Leybold separates three sizing questions: the effective pumping speed to reach a pressure in a given time, the speed to remove gas and vapour released continuously at operating pressure, and the speed to finish a process that produces vapour, such as drying. In the rough vacuum range, the speed needed for pump-down depends only on pressure, volume and time. [5]
Leybold warns that single-stage rotary vane and rotary piston pumps lose pumping speed below about 10 mbar with gas ballast and below 1 mbar without, and that the simple pump-down equations apply only when the ultimate pressure “is by several orders of magnitude lower than the desired pressure”. In its worked example, a 2,000 L vessel with a 120 s time constant reaches the target in about 18.5 min, which it rounds up to 25 min after adding reading uncertainty and a 20% safety factor. [5] [6]
As an editorial calculation example only, using the constant-speed relation t = (V/S)·ln(p₀/p): to take a 500 L chamber from 1,013 mbar to 10 mbar in 2 minutes needs about 0.5 m³ ÷ (2/60 h) × ln(101.3) ≈ 69 m³/h of effective speed at the chamber, before allowing for pipe conductance, leaks, outgassing and vapour.
Pfeiffer defines ultimate pressure as the pressure a blank-flanged pump approaches with no gas inlet, where usable pumping speed is zero; data sheets now give base pressure measured under ISO 21360-1. Choose a pump whose base pressure is well below the operating pressure. [3]
Give the chamber volume, target pressure and time, and the gas or vapour released during the process. A pump sized only for empty-chamber pump-down will stall when the product starts to release vapour.
04
Vacculex pairs screw, Roots and liquid ring pumps with customised vacuum systems; Souz and Value cover the liquid ring and rotary vane ends of the range. [7] [8] [9]
Baosi, for example, lists the GSD160B oil-free dry screw pump at 160 m³/h and 273 kg; Souz lists 2BV, 2BEA, 2BEC and 2SK liquid ring pumps alongside dry screw and scroll pumps; Value lists single- and two-stage rotary vane and VSP dry screw pumps. [10] [7] [9]
05
| Part | Role | Fix in the order |
|---|---|---|
| Rotor and vanes or screw rotors | Trap and compress gas; screw rotors run without contact or oil. [1] [2] | Pump principle, stages and rotor materials or coatings. |
| Housing or stator | Encloses the pumping chamber; dry screw housings are cooled at the outlet side. [2] | Material, cooling method and cooling water demand. |
| Inlet and outlet ports | Connect to the chamber and exhaust; Pfeiffer lists an inlet sieve and a silencer with non-return valve as standard equipment on its screw pumps. [2] | Flange sizes, inlet screen and exhaust silencer. |
| Gas ballast valve | Admits air or inert gas so vapour leaves before condensing. [4] [3] | Ballast flow and inert-gas option. |
| Oil, oil mist filter and separators (oil-sealed pumps) | Seal and lubricate; filters return oil and protect against dust and vapours. [1] | Oil type, mist filter and inlet traps. |
| Motor | Drives the pump; speed and base pressure depend on mains frequency. [1] | Power, voltage, frequency and enclosure. |
06
Four rows rest on Leybold and Pfeiffer notes: speed falling at low pressure, base pressure under ISO 21360-1, mains frequency and pump temperature. Motor power, noise, IP rating, mass and dimensions come only from the data sheet of the pump offered.
| Field | What it means and published values | Ask the supplier for |
|---|---|---|
| Pumping speed (m³/h) | Effective speed at the chamber sets pump-down time; speed falls at low pressure. [5] | Pumping-speed curve against inlet pressure. |
| Ultimate pressure (Pa) | Pfeiffer: “Today, base pressure is specified instead of ultimate pressure” (ISO 21360-1:2012); gas ballast raises it slightly. [3] | Base pressure with and without gas ballast. |
| Motor power (kW) | Rises with speed and compression. | Rated power and power at operating pressure. |
| Voltage (V) | Supply match. | Voltage range. |
| Frequency (Hz) | Speed and base pressure depend on mains frequency. [1] | Data at 50 Hz and 60 Hz. |
| Operating temperature (°C) | Pump temperature sets vapour handling. [4] | Ambient range and pump operating temperature. |
| Noise level (dB(A)) | Relevant for workplaces. | Sound level and test standard. |
| Ingress protection | Motor and electrical enclosure. | IP rating. |
| Weight (kg) | Needed for mounting. | Mass with motor and frame. |
| Dimensions (L×W×H) (mm) | Footprint and service access. | Dimensions and service clearances. |
07
Paste it into your enquiry below or into an email to a maker, then replace every bracket.
Gas: [all gases and vapours; quantities; water; solvents; acids; dust; flammable or toxic] Pressure: [operating pressure; lowest pressure; base pressure needed] Pump-down: [chamber volume; start and target pressure; required time] Gas load: [vapour or gas released during the process; leak rate] Type: [oil-sealed, dry screw, liquid ring, with or without Roots booster] Utilities: [voltage; frequency; cooling water; service liquid; exhaust routing] Accessories: [gas ballast or inert purge; inlet filter or trap; oil mist filter; silencer] Documents: [pumping-speed curve; base pressure and water-vapour tolerance; manual; ATEX if needed]
12 companies list this product among what they make. Company figures are quoted from each company's own website; every card states where the relationship came from.
Lists 2BV, 2BEA, 2BEC and 2SK liquid ring pumps, rotary vane, Roots, dry screw and scroll vacuum pumps.
Product scope checked 2026-10-10
Lists screw, Roots and liquid ring vacuum pumps and standard and customised vacuum systems.
Product scope checked 2026-10-10
Lists VSV single-stage and VRD two-stage rotary vane pumps and VSP dry screw vacuum pumps.
Product scope checked 2026-10-10
Lists GSD dry screw vacuum pumps, including the GSD160B at 160 m³/h, and single- and two-stage rotary vane pumps.
Product scope checked 2026-10-10
Lists rotary vane, piston, Roots and dry screw vacuum pumps, plus molecular pumps and vacuum fittings.
Product scope checked 2026-10-10
Lists vacuum pumps alongside its industrial air compressors.
Product scope checked 2026-10-10
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Water vapour condensing in the pump. Leybold and Pfeiffer explain that gas ballast lets vapour leave before it condenses; without it, condensate dissolves in the oil, raises base pressure and can corrode the pump. [4] [3]
Pfeiffer notes dry screw pumps run without oil in the pumping chamber and suit chemical, dusty or condensate-heavy processes; they have been replacing oil-sealed pumps in the 100–600 m³/h class. [2]
Sources checked 2026-10-12. Leybold and Pfeiffer Vacuum are vacuum pump manufacturers; their knowledge pages explain principles that apply across makes. Supplier pages describe their own offers. ISO 21360-1 and PNEUROP documents were not read for this page.
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