| Flooded Shell-and-Tube | Refrigerant surrounds the tubes; chilled water flows inside the tubes. | Approximately 30–80 kPa at design flow, depending on tube arrangement and flow rate. | Excellent Large refrigerant-side surface area and effective boiling provide strong thermal performance. | Excellent Generally maintains efficient refrigerant distribution at reduced load. | Tube brushing or mechanical cleaning is practical; requires oil-management and refrigerant-level control. | Tube leaks can allow refrigerant and water cross-contamination; low-flow and freeze protection are essential. | Large central water chillers, industrial cooling, and systems requiring high efficiency and serviceability. |
| Dry-Expansion Shell-and-Tube | Refrigerant expands inside tubes; chilled water flows over the outside of the tubes. | Approximately 30–80 kPa at design flow, subject to shell-side design and water velocity. | Good Reliable performance with a relatively simple refrigerant circuit. | Good Performance depends on expansion-valve control and maintaining adequate superheat. | Tube-side or shell-side cleaning is possible; water quality still strongly affects long-term capacity. | Water-side freezing can damage tubes; refrigerant distribution and oil return must be properly controlled. | Medium-to-large chillers where robust construction, straightforward operation, and cleanability are priorities. |
| Brazed-Plate Heat Exchanger | Refrigerant and chilled water pass through alternating corrugated plates separated by brazed joints. | Approximately 30–100 kPa, but higher pressure drop is common when compact sizing is prioritized. | Excellent High turbulence and close plate spacing enable high heat-transfer coefficients. | Good Compact refrigerant passages can perform efficiently, but control must prevent unstable flow. | Cannot normally be opened for mechanical cleaning; requires clean water, filtration, and chemical flushing when suitable. | Higher sensitivity Small passages increase blockage and freeze risk; leakage may require complete replacement. | Compact packaged chillers, small commercial systems, heat pumps, and applications with limited installation space. |
| Gasketed-Plate Heat Exchanger | Refrigerant and water flow through alternating channels formed by gasketed plates. | Approximately 40–120 kPa, depending on plate count, channel design, and selected approach temperature. | Excellent High surface-area density and close temperature approach are possible. | Good Effective at variable load when flow control and refrigerant distribution are correctly designed. | Easy to open and clean Gaskets require inspection and periodic replacement; plate tightening must follow the manufacturer’s procedure. | Gasket aging can cause external or internal leakage; freeze protection is still required on the water side. | Systems requiring compactness, inspectability, adjustable capacity, or frequent water-side cleaning. |
| Falling-Film Shell-and-Tube | Refrigerant is distributed over the outside of tubes and evaporates as a thin falling film; water flows inside tubes. | Approximately 30–80 kPa at design flow, depending on tube configuration. | Excellent Low refrigerant charge and efficient evaporation can support high seasonal efficiency. | Excellent Often suitable for efficient operation over a broad load range when distribution remains uniform. | Tube cleaning is practical, but refrigerant distributor maintenance and oil-return control are important. | Low refrigerant inventory can reduce some system risks, but inadequate wetting or low water flow may increase freeze risk. | Large high-efficiency chillers where reduced refrigerant charge and strong part-load performance are important. |