| Fixed-Plate Air-to-Air Heat Exchanger | Two separate air streams flow through alternating channels separated by thin plates. Heat passes through the plates while the streams remain isolated. | Supply air and exhaust air | Approximately 50–80% sensible effectiveness, depending on airflow balance, size, and channel design | Approximately 100–350 Pa per air path | Usually about −30°C to 80°C, subject to material and seal selection | Building ventilation, energy-recovery ventilation, clean-air systems, and industrial air exchange | No moving parts; low maintenance; no cross-contamination when properly sealed; compact construction | Cannot normally transfer moisture unless a permeable membrane is used; frost formation may require defrost or bypass control |
| Rotary Heat Recovery Wheel | A slowly rotating matrix alternately contacts the warm and cold air streams, storing and releasing heat as it rotates. | Supply air and exhaust air; sensible or total energy recovery with suitable matrix coatings | Approximately 65–85% sensible effectiveness; latent recovery depends on the matrix and coating | Approximately 150–400 Pa per air path | Commonly about −40°C to 60°C, depending on seal, rotor, and coating materials | Large commercial buildings, hospitals, airports, factories, and high-outdoor-air ventilation systems | High recovery efficiency; can recover sensible and latent energy; suitable for large airflow volumes | Contains moving parts; requires motor, seals, cleaning, and control; a small amount of carryover or leakage can occur |
| Heat Pipe Heat Exchanger | Sealed heat pipes use an internal working fluid that evaporates in the warm section and condenses in the cool section, transferring heat without a mechanical pump. | Two air streams separated by heat-pipe rows | Approximately 45–70% sensible effectiveness in typical air-handling applications | Approximately 100–300 Pa per air path | Often about −40°C to 80°C, depending on working fluid and casing materials | Ventilation heat recovery, data centers, humidity-control systems, and applications requiring separated air paths | No external power for heat transport; no cross-contamination between air streams; limited maintenance | Primarily sensible heat transfer; performance depends on orientation, airflow arrangement, and heat-pipe design |
| Finned-Tube Air-to-Liquid Coil | Air flows across extended metal fins attached to tubes carrying water, glycol solution, refrigerant, or another liquid. | Air-to-water, air-to-glycol, air-to-refrigerant, or air-to-thermal-oil | Performance is normally specified by heating or cooling capacity rather than a single effectiveness value; commonly selected using coil face velocity and design load | Approximately 50–250 Pa on the air side | Typically about −40°C to 150°C, depending on tube, fin, fluid, and seal materials | Air-conditioning units, process-air heating, cooling coils, heat pumps, and refrigeration systems | Widely available design formats; scalable capacity; suitable for heating, cooling, and dehumidification | Requires a liquid or refrigerant circuit; fin fouling reduces performance; condensate management may be necessary for cooling duty |
| Plate-Fin Air-to-Air Exchanger | Layered plates and fins create separate flow passages for two air streams, increasing surface area and turbulence for heat transfer. | Two air streams or air and another gas | Approximately 50–80% sensible effectiveness, depending on fin geometry and flow arrangement | Approximately 150–600 Pa per flow path | Often about −50°C to 200°C, depending on alloy, brazing, and sealing method | Aerospace systems, gas processing, industrial gas cooling, and compact high-performance equipment | High surface-area-to-volume ratio; compact and lightweight; suitable for demanding temperature duties | More sensitive to fouling and blockage; cleaning can be difficult; manufacturing and repair may be more specialized |
| Shell-and-Tube Air Cooler | Process fluid travels inside tubes while ambient or forced air flows over the external tube surfaces, usually with extended fins. | Process liquid or gas-to-air | Capacity is determined by overall heat-transfer coefficient, surface area, airflow, and temperature approach rather than a fixed effectiveness value | Approximately 100–500 Pa on the air side, excluding fan system losses | Commonly about −40°C to 250°C, with higher temperatures possible using specialized materials | Petrochemical processing, power generation, industrial cooling, and outdoor process equipment | Robust construction; suitable for large process duties; no cooling-water circuit required on the air side | Large footprint for high capacity; fan power and ambient conditions strongly affect performance; noise control may be required |
| Crossflow Air-to-Air Exchanger | Two air streams move approximately perpendicular to each other through separate passages divided by heat-transfer surfaces. | Supply air and exhaust air | Approximately 40–70% sensible effectiveness in typical non-condensing designs | Approximately 100–350 Pa per air path | Usually about −30°C to 80°C, depending on construction materials | Compact ventilation units, residential systems, small commercial buildings, and equipment enclosures | Simple airflow arrangement; compact height; easy integration into packaged ventilation equipment | Generally less effective than counterflow designs at the same size; frost and condensate control may be needed |
| Counterflow Air-to-Air Exchanger | Two air streams travel in opposite directions through adjacent channels, maintaining a favorable temperature difference across most of the exchanger length. | Supply air and exhaust air | Approximately 70–90% sensible effectiveness in well-designed systems | Approximately 150–500 Pa per air path | Commonly about −40°C to 80°C, subject to seals and construction materials | High-efficiency ventilation, cold-climate buildings, laboratories, and energy-recovery air-handling units | High thermal effectiveness; good temperature approach; strong energy-saving potential | Longer flow path can increase pressure drop; frost protection and condensate drainage may be required in cold or humid conditions |
| Evaporative Air Cooler | Air is cooled by water evaporation, either directly into the airstream or indirectly through a heat-transfer surface that keeps the air streams separated. | Air and water; indirect systems use separate air paths | Direct systems can achieve approximately 70–90% of the wet-bulb temperature difference; indirect performance varies by design | Approximately 50–250 Pa, excluding external duct and fan losses | Most effective in dry climates; operating limits depend on water quality, freezing risk, and equipment materials | Industrial ventilation, agricultural buildings, warehouses, data-center pre-cooling, and dry-climate comfort cooling | Low electrical energy use compared with compressor cooling; effective during hot and dry weather | Consumes water; adds humidity in direct systems; performance decreases at high ambient humidity; water treatment and hygiene control are important |