| General laboratory vacuum transfer | Oil-free diaphragm pump | 0.5–10 m³/h | Approximately 1–10 mbar absolute | Air, inert gases, and moderate chemical vapors; confirm elastomer compatibility | Vacuum filter and condensate trap | Avoid continuous condensation unless the pump is designed for it | Clean operation, low maintenance, chemical resistance, and noise level |
| Solvent evaporation and rotary evaporation | Chemical-resistant diaphragm pump | 1–8 m³/h | Approximately 1–5 mbar absolute | Organic vapors and corrosive gases, subject to wetted-material selection | Cold trap or solvent condenser upstream of the pump | Keep vapor temperature within the pump’s rated inlet range; prevent liquid slugging | Chemical resistance, vapor-handling capacity, ultimate pressure, and solvent recovery |
| High-flow air evacuation | Oil-lubricated rotary vane pump or dry scroll pump | 10–100 m³/h | Approximately 0.001–1 mbar absolute | Dry air and inert gases; oil-sealed designs require contamination control | Inlet screen, particulate filter, and suitable exhaust filtration | Use gas ballast or equivalent moisture-management features when required | Pump-down time, continuous-duty rating, ultimate pressure, and operating cost |
| Food, pharmaceutical, and hygienic transfer | Dry claw, dry screw, or oil-free diaphragm pump | 10–250 m³/h | Approximately 0.1–100 mbar absolute, depending on design | Air and process gases; select materials compatible with cleaning agents | Sanitary inlet filter, liquid separator, and cleanable piping | Consider washdown, condensate, and cleaning-cycle temperatures | Oil-free compression, cleanability, drainage, hygienic materials, and validation requirements |
| Vacuum packaging | Rotary vane, dry claw, or dry scroll pump | 20–300 m³/h | Approximately 0.5–10 mbar absolute | Air and food-related vapors; oil-free operation may be preferred | Product filter, liquid separator, and optional bacterial filter | Manage moisture and product vapor to avoid corrosion or performance loss | Cycle time, peak flow, moisture tolerance, footprint, and service intervals |
| Liquid transfer and priming | Liquid-ring pump or vacuum-assisted centrifugal system | 10–500 m³/h | Typically 30–100 mbar absolute, depending on liquid temperature | Wet gases and entrained liquids; liquid compatibility is essential | Liquid separator, non-return valve, and appropriately sized inlet piping | Water vapor pressure limits the achievable vacuum; hot liquids reduce performance | Liquid compatibility, seal design, priming time, cooling-water demand, and corrosion resistance |
| Dusty or abrasive material handling | Dry claw or rotary lobe pump with robust filtration | 20–500 m³/h | Approximately 10–200 mbar absolute | Air and dry process gases; protect the pump from abrasive solids | High-efficiency cyclone, cartridge filter, or bag filter with differential-pressure monitoring | Prevent overheating caused by blocked filters or restricted airflow | Filter area, dust-loading capacity, wear resistance, cleanout method, and shutdown protection |
| Continuous industrial vacuum service | Dry screw, dry claw, rotary vane, or liquid-ring pump | 50–2,000 m³/h | Approximately 0.1–500 mbar absolute, depending on pump technology | Select according to gas composition, moisture level, dust content, and corrosion risk | Process-specific filtration, separators, condensers, and check valves | Verify ambient, gas, cooling, and discharge temperature limits | Total cost of ownership, redundancy, energy consumption, controls, uptime, and maintenance access |