| Rotary drum screen | Influent passes through a rotating perforated or wedge-wire drum; retained solids are lifted and discharged. | Approximately 0.25–3 mm opening size | About 20–1,000 m³/h, depending on screening aperture and solids loading | Municipal wastewater, food processing, aquaculture, industrial pre-treatment, irrigation-water intake | US$5,000–80,000 for standard equipment; larger packaged systems cost more | EN 12255-3 where applicable; ISO 12100; IEC 60204-1; IEC 60529; ATEX requirements if installed in a hazardous area | Verified hydraulic test data, corrosion-resistant construction, accessible spray-bar design, local spare-parts support | Inspect screen surface weekly; clean spray nozzles; check seals, bearings, chain or gearbox, and differential level controls monthly | Screen blinding, undersized discharge conveyor, high-pressure wash-water demand, corrosion at welds |
| Rotary disc filter | Water flows through rotating filter panels; solids accumulate on the media and are removed by backwash sprays. | Typically 10–100 µm, depending on media and process conditions | About 50–3,000 m³/h for tertiary-water applications | Tertiary wastewater treatment, water reuse, cooling-water polishing, aquaculture and process-water clarification | US$20,000–250,000, excluding civil works and major control-system integration | ISO 12100; IEC 60204-1; IEC 60529; local wastewater discharge or reclaimed-water requirements; NSF/ANSI/CAN 61 where applicable to potable-water contact | Independent performance testing, clear net-area calculations, documented backwash-water consumption, replaceable media panels | Check panel fouling and spray pressure weekly; inspect drive, shaft, seals, and level sensors monthly; deep-clean media as required | Actual flow may fall sharply with high suspended solids; poor panel access; excessive backwash-water use |
| Automatic self-cleaning screen filter | Pressurized liquid passes through a cylindrical screen; an internal scanner or suction assembly removes retained particles automatically. | Approximately 20–3,000 µm | About 5–2,000 m³/h, depending on mesh size and water quality | Irrigation, cooling towers, membrane pre-treatment, industrial process water, pump protection | US$2,000–100,000 per unit, depending on diameter, material, automation, and pressure rating | Pressure-equipment rules where applicable; ISO 12100; IEC 60204-1; IEC 60529; NSF/ANSI/CAN 61 where applicable | Pressure-loss curves, minimum flush-flow data, screen-area calculations, electrical compatibility, availability of seals and screens | Monitor differential pressure; inspect screen and scanner monthly; verify flushing valves, actuators, and control logic quarterly | Incorrect mesh selection, insufficient flush pressure, control-panel incompatibility, unplanned downtime during screen replacement |
| Rotary vacuum drum filter | A rotating drum partially submerged in slurry forms a filter cake under vacuum; the cake is dewatered and discharged continuously. | Approximately 5–200 µm equivalent separation, strongly dependent on cake properties | About 1–100 m³/h of slurry feed, depending on solids concentration | Mineral processing, chemicals, food ingredients, sludge dewatering, and industrial solids recovery | US$30,000–300,000, excluding vacuum pumps, cake conveyors, and building services | ISO 12100; IEC 60204-1; pressure and hazardous-area requirements where applicable; food-contact rules where applicable | Pilot-test results with the buyer’s slurry, documented cake-moisture data, vacuum-pump sizing, material compatibility, and wear-part availability | Inspect filter cloth, scraper, vacuum seals, drum bearings, and filtrate lines; replace cloth according to wear and blinding condition | Performance varies greatly with particle shape and cake permeability; vacuum leakage; cloth blinding; high installation complexity |
| Centrifugal separator | Rotational flow creates centrifugal force that separates denser solids or liquid phases from the carrier fluid. | Commonly about 5–100 µm for hydrocyclonic or centrifugal solid separation; actual cut size depends on density and viscosity | About 5–500 m³/h for industrial liquid-solid separation | Sand removal, cooling-water protection, machine-tool fluids, process liquids, and pre-treatment before fine filtration | US$1,500–75,000, depending on pressure, materials, automation, and solids-discharge method | ISO 12100; IEC 60204-1; pressure-equipment requirements where applicable; ATEX requirements for classified areas | Verified separation curve, minimum operating pressure, wear-resistant liners, automatic purge option, and density assumptions | Check purge outlet and wear surfaces weekly; inspect pressure gauges, valves, liners, and supports; flush accumulated solids as needed | Cannot reliably remove particles with insufficient density difference; abrasive wear; pressure loss; incorrect flow-rate assumptions |
| Rotary pressure filter | A rotating filter element operates inside a pressurized housing, allowing continuous filtration and solids discharge. | Approximately 1–50 µm, depending on media and process conditions | About 1–150 m³/h for process liquids or slurries | High-value process fluids, pigment and chemical production, oils, polymers, and continuous solids removal | US$40,000–350,000, excluding upstream pumps, instrumentation, and hazardous-area upgrades | Applicable pressure-equipment legislation; ISO 12100; IEC 60204-1; IEC 60529; ATEX or IECEx requirements where specified | Pressure-vessel design records, factory pressure testing, material certificates, seal compatibility, and documented clean-in-place capability | Monitor pressure differential and leakage; inspect seals, bearings, drive train, filter media, and discharge mechanism on a scheduled basis | High capital cost, complex sealing, difficult access to internal parts, and potentially long lead times for custom components |