| Finned-Tube DX Evaporator | Copper tubes with aluminum fins are common. Aluminum tubes and fins may also be used in all-aluminum designs. | Direct-expansion circuit with multiple tubes, return bends, fins, and an air-side fan. Tube spacing can be adjusted for clean or frost-prone air. | R-134a R-404A R-407C R-410A R-448A/R-449A R-454C Also suitable for other HFC/HFO blends when the coil, oil, seals, and safety classification are approved. | Good air-side performance and flexible circuiting. Frost formation can significantly reduce airflow and capacity, so defrost strategy and fin spacing are important. | Versatile, widely available, easy to configure for different air temperatures, and suitable for many air-cooling duties. | Copper is generally unsuitable for ammonia service. Aluminum components require corrosion protection in aggressive or saline atmospheres. Refrigerant distribution must be designed carefully to avoid maldistribution and poor superheat control. | Cold rooms, display cases, air handlers, blast chillers, process-air coolers, and comfort-cooling equipment. |
| All-Aluminum Microchannel Evaporator | Aluminum flat multiport tubes, aluminum fins, and aluminum headers. | Compact parallel-flow or multiport passages with a high external surface-area-to-volume ratio. | R-134a R-410A R-32 R-454B R-454C Also used with selected HFO/HFC blends and carbon dioxide only when specifically pressure-rated and engineered for that duty. | High compactness and low internal refrigerant volume. Performance is sensitive to refrigerant distribution, circuit arrangement, and fouling on the air side. | Compact size, reduced material volume, low refrigerant charge potential, and good air-side heat transfer. | More difficult to clean internally, less tolerant of mechanical damage, and vulnerable to galvanic or chemical corrosion. Standard aluminum microchannel construction is not a default choice for ammonia. | Packaged air-conditioning units, heat pumps, transport cooling, and space-constrained air-cooling equipment. |
| Brazed Plate Heat Exchanger | Stainless-steel corrugated plates joined by copper or nickel-based brazing, depending on the refrigerant and service requirements. | Compact counterflow plate pack with refrigerant on one side and water, glycol, or another secondary fluid on the other side. | HFC/HFO blends R-717 ammonia* R-744 CO₂* R-290 propane* Compatibility depends on plate material, braze alloy, pressure rating, oil, and the manufacturer’s approval. | High heat-transfer coefficients and close temperature approach are possible. Pressure drop can rise quickly at high flow rates or with narrow channels. | Very compact, efficient, low hold-up volume, and well suited to liquid-to-refrigerant evaporating duties. | Internal fouling is difficult to remove mechanically. Freezing, rapid pressure transients, or poor water treatment can damage plates. Ammonia service requires a construction specifically approved for ammonia; copper-brazed units should not be assumed compatible. | Chillers, heat pumps, secondary-loop systems, process cooling, and domestic or commercial hot-water heat pumps. |
| Shell-and-Tube Evaporator | Carbon-steel or stainless-steel shell with copper, cupronickel, stainless-steel, or titanium tubes, selected according to fluid chemistry and pressure requirements. | Flooded or DX shell-and-tube arrangement. The refrigerant may boil inside tubes or on the shell side, depending on the design. | R-717 ammonia R-744 CO₂* HFC/HFO blends Material selection is critical: copper and ammonia are generally incompatible, while stainless steel is commonly considered for ammonia circuits. | Robust construction, stable operation, and good suitability for large water or glycol flows. Flooded designs can provide high evaporating-side performance but require reliable oil management. | Durable, serviceable, scalable, and suitable for industrial capacities and dirty or treated secondary fluids. | Larger footprint and refrigerant charge than compact plate units. Tube fouling, corrosion, freezing, and refrigerant-side oil return must be addressed during design. | Industrial chillers, large process systems, central refrigeration plants, and marine or heavy-duty cooling systems. |
| Flooded Evaporator | Usually shell-and-tube or shell-and-coil construction using steel, stainless steel, or other verified alloys. | Refrigerant level is maintained so the heat-transfer surface remains wetted; a separator or surge vessel is often included. | R-717 ammonia R-134a R-513A R-1234ze(E) Can be used with other refrigerants when the vessel, controls, oil, and materials are appropriately rated. | High evaporating-side heat-transfer performance and low superheat across much of the surface. Requires level control, oil return management, and protection against liquid carryover. | Efficient at large capacities, stable outlet temperature, and good performance with relatively small temperature approaches. | More components and controls than a simple DX system. Liquid carryover can damage compressors, and refrigerant charge may be comparatively high. | Large chillers, industrial refrigeration, process cooling, and systems with steady thermal loads. |
| Immersed Coil Evaporator | Stainless steel, carbon steel, titanium, or other alloy tubing immersed in a tank or vessel. Copper may be used only where fluid compatibility is confirmed. | Coils are submerged in water, brine, glycol, or a process liquid; refrigerant may circulate inside the coil. | R-717 ammonia* HFC/HFO blends R-744 CO₂* The fluid being cooled and the coil metallurgy must both be checked, especially for brines, food liquids, and corrosive solutions. | Provides thermal buffering and can reduce short cycling. Heat transfer depends strongly on liquid movement, coil arrangement, fouling, and tank mixing. | Simple concept, good thermal inertia, low air-side maintenance, and useful for batch or process cooling. | Large tank volume, slower response than direct air cooling, potential biological or mineral fouling, and difficult access for cleaning. | Ice banks, beverage cooling, process tanks, glycol systems, and agricultural or food-processing applications. |
| Plate-and-Frame Evaporator | Stainless-steel plates with elastomeric gaskets; plate alloys and gasket materials vary with fluid and temperature. | Demountable gasketed plates arranged for counterflow heat exchange between refrigerant and a secondary fluid. | HFC/HFO blends R-717 ammonia* Refrigerant use requires a design specifically rated for two-phase service, pressure, gasket compatibility, and the selected refrigerant. | High heat-transfer coefficients and adjustable surface area. Two-phase flow distribution and gasket performance require careful design. | Openable for inspection and cleaning, capacity can be expanded, and close temperature approaches are achievable. | Gaskets age with temperature and chemical exposure. Not all gasketed plate units are suitable for refrigerant duty, high pressure, flammable refrigerants, or vacuum conditions. | Large water-to-refrigerant systems, process chillers, district cooling, and installations requiring cleanability. |
| Evaporative Surface or Falling-Film Evaporator | Stainless steel, nickel alloys, or other corrosion-resistant materials selected for the process fluid and refrigerant. | Refrigerant evaporates on or within a wetted heat-transfer surface while a liquid film flows over the surface. | HFC/HFO blends R-717 ammonia R-744 CO₂* Exact compatibility depends on pressure, metallurgy, lubrication, seals, and the specific falling-film arrangement. | Can achieve high surface utilization and low refrigerant inventory in suitable designs. Performance depends on maintaining uniform wetting and preventing dry areas. | Potentially low charge, efficient heat transfer, and good suitability for large industrial duties. | Sensitive to distribution, oil contamination, fouling, and operating transients. Requires sophisticated control and commissioning. | Industrial chillers, large process systems, low-charge refrigeration, and applications with stable liquid circulation. |