Abstract
Improving the heat transfer performance of falling film evaporators is a crucial step for improving the energy efficiency of the heat pump or refrigeration systems. This study conducts a numerical investigation for the practical-scale falling film evaporator based on the epsilon–NTU method with an updated heat transfer correlation. The algorithm was validated with lab-scale and real-scale falling film evaporator experimental results, and the prediction reaches a mean absolute deviation of 12.5%. The parametric study encompasses eight refrigerants: R-134a, R-410A, R-600a, R-717, R-1270, R-152a, R-1234yf, and R-1234ze(E). The results indicate that vaporization enthalpy of refrigerant is a key property in selecting an appropriate working fluid because it helps minimize severe heat transfer degradation caused by dry-out. Additionally, the vapor-flow–induced heat transfer degradation can be predicted using the critical Weber number. Furthermore, the trade-off between extending the tube length and increasing the number of tubes for heat transfer improvement is discussed. Finally, different two-pass arrangements show deviations of less than 4 %.
| Original language | English |
|---|---|
| Article number | 120743 |
| Journal | Energy Conversion and Management |
| Volume | 348 |
| DOIs | |
| State | Published - Jan 15 2026 |
Funding
The authors acknowledge the support provided by US Department of EnergyBuilding Technologies Office (BTO). This research used resources at the Building Technologies Research and Integration Center, a DOE Office of Science User Facility operated by the Oak Ridge National Laboratory. Financial support from National Science and Technology Council Taiwan under the contract NSTC 112-2221-E-A49-026 is also acknowledged.
Keywords
- Dry-out
- Falling film evaporator
- Modeling
- Nucleate boiling
- Vapor flow