Metal-Hydride-Based Hydrogen Storage as Potential Heat Source for the Cold Start of PEM FC in Hydrogen-Powered Coaches: A Comparative Study of Various Materials and Thermal Management Techniques
Abstract
:1. Introduction
2. Methodology
2.1. Tank Geometries and Thermal Management Scenarios
2.2. Numerical Model
2.2.1. Assumptions of the Numerical Model
- (a)
- The medium is in a local thermal equilibrium, which implies that there is no heat transfer between solid and gas phases.
- (b)
- The temperature and pressure profiles are initially uniform.
- (c)
- Hydrogen is treated as an ideal gas from a thermodynamic point of view. This is an assumption that sometimes might be far from the reality and might affect the accuracy of the model. In case the hydrogen pressure is below 20 bar and room temperature, this is, in general, an acceptable assumption supported by the literature [34,35,36]. However, this assumption must not be made when the pressure of the system is higher. For the analysis of a hydride-based hydrogen compressor, the compressibility factor must be considered when the density of the gas is calculated and updated [15]. Just for the comparison, the compressibility factor for a pressure of 20 bar, temperature of 10 °C and 100 g H2 is Z = 1.079804 whereas for pressure of 300 bar (middle stage for a 700 bar compressor) the compressibility factor is Z = 1.25 [37]. (The compressibility factor for ideal gas is 1.)
- (d)
- Thermal conductivity and specific heat capacity are assumed to be constant.
- (e)
- The porosity remains constant and uniform during hydrogenation.
- (f)
- The characteristics (the kinetics and thermal properties) of the bed are unaffected by the number of loading and unloading cycles. Thus, bed aging is neglected.
- (g)
- The metal hydride bed fills the entire space between the cooling tubes and the spiral heat exchanger (perfect packing condition).
2.2.2. Heat Equation
2.2.3. Hydrogen Mass Balance
2.2.4. Momentum Equation
2.2.5. Hydrogenation Kinetic Expression
2.2.6. Equilibrium Pressure
3. Validation of the Numerical Model
4. Results and Discussion
4.1. Temperature Distribution and Hydrogenation Kinetics
4.2. Thermal Coupling of the Metal Hydride and the PEMFC
5. Conclusions
Supplementary Materials
Author Contributions
Funding
Conflicts of Interest
References
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Thermal Management Scenario | No Cooling Tubes | Spiral Coil | Tank Radius (m) | Tank Length (m) | Active Surface Area (m2) |
---|---|---|---|---|---|
Scenario 1 | 4 | No | 0.0517 | 0.5 | 0.0952 |
Scenario 2 | 6 | No | 0.0517 | 0.5 | 0.1269 |
Scenario 3 | 1 | Yes | 0.0517 | 0.5 | 0.1037 |
Scenario 4 | 4 | Yes | 0.0517 | 0.5 | 0.1671 |
Scenario 5 | 6 | Yes | 0.0517 | 0.5 | 0.2147 |
Properties | LaNi5 | Mm Intermetallic | AB2 Intermetallic |
---|---|---|---|
Effective density (kg/m3) | 4175.0 | 3172.5 | 3250.0 |
Activation Energy (J/molH2) | 28,500.0 | 26,250.0 | 24,350.0 |
Enthalpy of formation (J/molH2) | 28,300.0 | 25,242.0 | 28,579.0 |
Entropy of formation (J/molH2/K) | 102.1 | 105.1 | 106.8 |
Molecular weight (g/mol) | 432.5 | 435.2 | 173.9 |
N/A | AB2 Intermetallic ts (s) | LaNi5 ts (s) | Mm AB5 Intermetallic ts (s) |
---|---|---|---|
Scenario 1 | 1340 | 2051 | 2495 |
Scenario 2 | 1070 | 1785 | 1950 |
Scenario 3 | >2500 | >2500 | >2500 |
Scenario 4 | 1250 | 1850 | 2179 |
Scenario 5 | 890 | 1410 | 1560 |
N/A | AB2 Intermetallic Total Mass (kg) | LaNi5 Total Mass (kg) | Mm AB5 Intermetallic Total Mass (kg) |
---|---|---|---|
Scenario 1 | 10.52 | 11.79 | 11.73 |
Scenario 2 | 10.85 | 12.11 | 12.05 |
Scenario 3 | 10.35 | 11.61 | 11.56 |
Scenario 4 | 10.83 | 12.11 | 12.04 |
Scenario 5 | 11.16 | 12.42 | 12.36 |
Parameter | Unit | Value |
---|---|---|
Inner mass | kg | 175 |
Block mass | kg | 175 |
Head mass | kg | 67 |
Fluid volume in fuel cell | L | 0.5 |
Heat transfer area | m2 | 8 |
Convective heat transfer coeff. | Wm−2K−1 | 1000 |
Area for external convection to ambient | m2 | 1 |
Convective heat transfer coeff. to ambient | Wm−2K−1 | 50 |
Case | Cold Start Time (s) | Reduced Time (%) |
---|---|---|
No MH | 623 | 0 |
AB2—Scenario 2 | 578 | 7.23 |
AB2—Scenario 5 | 572 | 8.19 |
LaNi5—Scenario 5 | 595 | 4.49 |
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Gkanas, E.I.; Wang, C.; Shepherd, S.; Curnick, O. Metal-Hydride-Based Hydrogen Storage as Potential Heat Source for the Cold Start of PEM FC in Hydrogen-Powered Coaches: A Comparative Study of Various Materials and Thermal Management Techniques. Hydrogen 2022, 3, 418-432. https://doi.org/10.3390/hydrogen3040026
Gkanas EI, Wang C, Shepherd S, Curnick O. Metal-Hydride-Based Hydrogen Storage as Potential Heat Source for the Cold Start of PEM FC in Hydrogen-Powered Coaches: A Comparative Study of Various Materials and Thermal Management Techniques. Hydrogen. 2022; 3(4):418-432. https://doi.org/10.3390/hydrogen3040026
Chicago/Turabian StyleGkanas, Evangelos I., Chongming Wang, Simon Shepherd, and Oliver Curnick. 2022. "Metal-Hydride-Based Hydrogen Storage as Potential Heat Source for the Cold Start of PEM FC in Hydrogen-Powered Coaches: A Comparative Study of Various Materials and Thermal Management Techniques" Hydrogen 3, no. 4: 418-432. https://doi.org/10.3390/hydrogen3040026
APA StyleGkanas, E. I., Wang, C., Shepherd, S., & Curnick, O. (2022). Metal-Hydride-Based Hydrogen Storage as Potential Heat Source for the Cold Start of PEM FC in Hydrogen-Powered Coaches: A Comparative Study of Various Materials and Thermal Management Techniques. Hydrogen, 3(4), 418-432. https://doi.org/10.3390/hydrogen3040026