Review and Evaluation of Hydrogen and Air Heat Exchangers for Fuel Cell-Powered Electric Aircraft Propulsion †
Abstract
:1. Introduction
2. Methodology
2.1. Application Area in the Context of Electric Aviation
2.2. Criteria for Weighting
2.3. Selection Criteria
2.3.1. Thermal Performance
2.3.2. Compactness and Weight
2.3.3. Pumping Power
2.3.4. Design Flexibility
2.3.5. Reliability and Life Cycle Cost
2.3.6. Development and Manufacturing Cost
3. Results and Discussion
3.1. Selection Criteria for Air HEX
3.2. Selection Criteria for Hydrogen HEX
3.3. Heat Exchanger Type Rating for Air and Hydrogen HEX
3.4. Potential and Challenges for HEXs in Aviation
4. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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Criterion | T | CW | P | DF | RL | DM | Weight |
---|---|---|---|---|---|---|---|
Thermal Performance (T) | - | 2 | 2 | 2 | 1 | 2 | 0.300 |
Compactness and Weight (CW) | 0 | - | 1 | 2 | 0 | 2 | 0.167 |
Pumping Power (P) | 0 | 1 | - | 2 | 0 | 2 | 0.167 |
Design Flexibility (DF) | 0 | 0 | 0 | - | 1 | 1 | 0.067 |
Reliability and Life Cycle Cost (RL) | 1 | 2 | 2 | 1 | - | 2 | 0.267 |
Development and Manufacturing Cost (DM) | 0 | 0 | 0 | 1 | 0 | - | 0.033 |
Criterion | T | CW | P | DF | RL | DM | Weight |
---|---|---|---|---|---|---|---|
Thermal Performance (T) | - | 2 | 2 | 1 | 0 | 2 | 0.233 |
Compactness and Weight (CW) | 0 | - | 2 | 0 | 0 | 2 | 0.133 |
Pumping Power (P) | 0 | 0 | - | 0 | 0 | 2 | 0.067 |
Design Flexibility (DF) | 1 | 2 | 2 | - | 1 | 1 | 0.233 |
Reliability and Life Cycle Cost (RL) | 2 | 2 | 2 | 1 | - | 2 | 0.300 |
Development and Manufacturing Cost (DM) | 0 | 0 | 0 | 1 | 0 | - | 0.033 |
Criteria | Extended Surface [4,7,16,17,18] | TPMS [9,19] | MCHE [5,8,16,20,21] | Plate [4,5,7,8,21] | PCHE [4,6,22,23] |
---|---|---|---|---|---|
Thermal Performance | High heat transfer and surface area due to fins | Superior heat transfer due to intricate path that enhances turbulence | Excellent thermal performance due to small hydraulic diameter | Moderate performance due to corrugated and tortuous channels | High thermal performance due to fine grooves and bending channels |
+ | ++ | ++ | o | + | |
Compactness and Weight | High compactness up to 4500 m2/m3 | Very high compactness up to 7500 m2/m3 | Very high compactness up to 7500 m2/m3 achieved | Moderate compactness till 600 m2/m3 | Lower compactness than plate and tube fin, up to 2500 m2/m3 |
+ | ++ | ++ | - | o | |
Pumping Power | Moderate pumping power, depending on fin density and arrangement | Complex internal geometry results in very high friction factors | High pumping power due to small hydraulic diameter and enhanced viscous effects | High losses due to highly interrupted and narrow passages | High losses due to complex paths and flow disruptions |
+ | - - | - | - | - | |
Design Flexibility | Highly versatile, can handle various fluids, temperatures, and pressures. Compatible with different materials. | Innovative but limited flexibility. Challenging to manufacture, restricted to specific materials and applications | Specialized for specific applications, less adaptable to different fluids and configurations. Limited material options due to precision requirements | Offers good flexibility with various fluids and operating conditions. Gasketed types are highly adaptable, while brazed and welded types are more robust but less flexible | Good for high pressures and temperatures. Slightly less flexible in fluid and material choices (Carbon steel not used) |
++ | o | o | + | + | |
Reliability and Life Cycle Cost | Low fouling risk and minimal leakage at joints due to a robust design with fins providing structural strength. Regular inspection and cleaning are required to prevent blockages. | Prone to fouling, traps particles, moderate leakage risk. Limited data on long-term performance in harsh environments. | Good resistance to fouling with moderate leakage risk due to thin walls and complex manufacturing. Robust design with regular maintenance is needed due to blockages | Good reliability due to mature technology. Gasketed designs offer easy maintenance, while brazed/welded types withstand harsher conditions | Extremely reliable, especially in high-pressure and temperature environments, with low leakages and fouling. Diffusion bonding minimizes thermal distortion. |
+ | o | o | + | ++ | |
Development and Manufacturing Cost | High TRL level, already used in aviation, moderate manufacturing cost based on fin design and material used | No correlations for air and hydrogen present, very high cost due to additive manufacturing | Air and hydrogen are not the common media used, high manufacturing costs (laser micro-machining) | High TRL level, moderate manufacturing cost per heat-transfer surface area | Simulation, and experiment results are not available for air, hydrogen. Very high manufacturing cost due to diffusion bonding |
++ | - - | - | + | - - | |
Relative Rating for Air HEX | 0.775 | 0.633 | 0.683 | 0.508 | 0.667 |
Relative Rating for Hydrogen HEX | 0.816 | 0.633 | 0.658 | 0.591 | 0.733 |
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Bhapkar, S.; Sain, C.; Kazula, S. Review and Evaluation of Hydrogen and Air Heat Exchangers for Fuel Cell-Powered Electric Aircraft Propulsion. Eng. Proc. 2025, 90, 62. https://doi.org/10.3390/engproc2025090062
Bhapkar S, Sain C, Kazula S. Review and Evaluation of Hydrogen and Air Heat Exchangers for Fuel Cell-Powered Electric Aircraft Propulsion. Engineering Proceedings. 2025; 90(1):62. https://doi.org/10.3390/engproc2025090062
Chicago/Turabian StyleBhapkar, Sahil, Chetan Sain, and Stefan Kazula. 2025. "Review and Evaluation of Hydrogen and Air Heat Exchangers for Fuel Cell-Powered Electric Aircraft Propulsion" Engineering Proceedings 90, no. 1: 62. https://doi.org/10.3390/engproc2025090062
APA StyleBhapkar, S., Sain, C., & Kazula, S. (2025). Review and Evaluation of Hydrogen and Air Heat Exchangers for Fuel Cell-Powered Electric Aircraft Propulsion. Engineering Proceedings, 90(1), 62. https://doi.org/10.3390/engproc2025090062