Effects of Cell Design Parameters on Zinc-Air Battery Performance
Abstract
:1. Introduction
1.1. Overview of Zn-Air Batteries
1.2. Electrolyte Additives
1.3. Bifunctional Catalyst for Air Electrode
1.4. Surface Morphology of Air Electrode
1.5. Effects of Air Electrode Catalyst on Cell Power Density
1.6. Effects of Zinc Type on Cell Power Density
1.7. Effect of Cell Configuration on Power Density
1.8. Motivation and Scope of Present Study
- Cell 1 (proximity cell): electrodes are in close proximity (less than 1 mm),
- Cell 2 (aqueous electrolyte cell): equal-area electrodes separated with aqueous electrolyte,
- Cell 3 (cathode limited cell): large zinc electrode area and small air electrode area,
- Cell 4 (air flow channel cell): channel flow on the air side.
2. Experimental and Computer Modeling
2.1. Configuration of Cells under Investigation
2.2. Configuration of Cells under Investigation—Cell 1
2.3. Configuration of Cells under Investigation—Cell 2
2.4. Configuration of Cells under Investigation—Cell 3
2.5. Configuration of Cells under Investigation—Cell 4
2.6. Modified 25BC Carbon Paper as Cathode
2.7. Computer Modeling of Testing Cells—Current Distribution
3. Results and Discussion
3.1. Cell 1
3.2. Cell 2
3.3. Cell 3
3.4. Cells 4a–c
3.5. Volumetric Power Density Versus Power Density Based on Cathode Area
4. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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Factor | Modified ORR Electrode | Forced Air Convection | Anode/Cathode Area Ratio | Anode/Cathode Distance | |
---|---|---|---|---|---|
Cell Type | |||||
Cell 1 | ○ | ○ | △ | ||
Cell 2 | ○ | ○ | △ | ||
Cell 3 | ○ | ○ | ○ | △ | |
Cell 4 | ○ | ○ & △ |
c_bulk | Reactant bulk concentration | 1600 [mmol/L] |
Cdl | Double layer capacitance | 0.5 [F/m^2] |
DA | Reactant diffusion coefficient | 3.5 × 10−9 [m^2/s] |
DB | Product diffusion coefficient | 3.5 × 10−9 [m^2/s] |
E_eqref1 | Equilibrium potential of RXN 1 | 1.25 [V] |
E_vertex1 | Start potential | 1.3 [V] |
E_vertex2 | Switching potential | 0.4 [V] |
i0ref1 | Reference exchange current density of RXN 1 | 1.0 × 10 [A/m^2] |
K0 | Reaction rate (dimensionless) | 1.00 × 1010 |
T | Temperature | 298.15 [K] |
v | Voltametric scan rate | 0.002 [V/s] |
L | Outer bound on diffusion layer | 6 × sqrt(DA × 2 × abs(E_vertex1 − E_vertex2)/v) |
cB0 | Initial product concentration at electrode | c_bulk/(1 + exp(−E_vertex1 × F_const/(R_const × T))) |
Alpha_a | Anodic charge transfer coefficient | 0.7 |
sigma_l | Electrolyte conductivity 65 S/m 6M KOH | 5.0 × 102 [S/m] |
T | Temperature | 25 + 273 [K] |
disp | Cathode displacement in parametric sweep | 0 [mm] |
a_H | Proton activity | 0.5 × 2 × 180 [g/dm3]/98.1 [g/mol]/(1 [mol/dm3]) |
c_Zn | Zinc concentration | 50 [g/dm3]/65.4 [g/mol] |
E_O2 | Equilibrium potential, Oxygen oxidation reaction | 1.229 [V] − R_const × T/(2 × F_const) × log(0.9/(1 × a_H^2)) |
E_Zn | Equilibrium potential, Zinc reaction | −0.763 [V] − R_const × T/(2 × F_const) × log(1/(0.1 × c_Zn/1 [mol/dm3])) |
E_H | Equilibrium potential, Hydrogen evolution | 0-R_const × T/(F_const) × log(1/a_H) |
i0_O2 | Exchange current density, Oxygen oxidation reaction | 0.1 × i0_Zn |
i0_Zn | Exchange current density, Zinc reaction | −1.0 × 10−7 [A/m^2] |
i0_H | Exchange current density, Hydrogen evolution | −1 × 10−11 [A/m^2] |
alphaa_O2 | Anodic transfer coefficient, Oxygen oxidation reaction | 2-alphac_O2 |
alphac_O2 | Cathodic transfer coefficient, Oxygen oxidation reaction | 0.6 |
alphaa_Zn | Anodic transfer coefficient, Zinc reaction | 1.1 |
alphac_Zn | Cathodic transfer coefficient, Zinc reaction | 2-alphaa_Zn |
phisext | External electric potential | 0.9 [V] |
Cell | Pmax, mW | Cathode Area (Acathode) cm2 | Pmax/Acathode | Velectrolyte | Pmax/Velectolyte | |||
---|---|---|---|---|---|---|---|---|
25BC | Modified 25BC | 25BC | Modified 25BC | cm3 | 25BC | Modified 25BC | ||
1 | 32.0 | 52.6 | 4.0 | 8 | 13.15 | 0.4 | 320.0 | 131.5 |
2 | 29.1 | 30.6 | 25.0 | 1.16 | 1.22 | 12.5 | 58.0 | 2.45 |
3 | 72.0 | 88.3 | 1.0 | 72.0 | 88.3 | 42.0 | 2.0 | 2.10 |
4a | 41.9 | 10.0 | 4.19 | 5.1 | 82.0 | |||
4b | 38.5 | 10.0 | 3.85 | 10.2 | 38.0 | |||
4c | 28.6 | 10.0 | 2.86 | 15.4 | 19.0 |
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Lu, C.-T.; Zhu, Z.-Y.; Chen, S.-W.; Chang, Y.-L.; Hsueh, K.-L. Effects of Cell Design Parameters on Zinc-Air Battery Performance. Batteries 2022, 8, 92. https://doi.org/10.3390/batteries8080092
Lu C-T, Zhu Z-Y, Chen S-W, Chang Y-L, Hsueh K-L. Effects of Cell Design Parameters on Zinc-Air Battery Performance. Batteries. 2022; 8(8):92. https://doi.org/10.3390/batteries8080092
Chicago/Turabian StyleLu, Cian-Tong, Zhi-Yan Zhu, Sheng-Wen Chen, Yu-Ling Chang, and Kan-Lin Hsueh. 2022. "Effects of Cell Design Parameters on Zinc-Air Battery Performance" Batteries 8, no. 8: 92. https://doi.org/10.3390/batteries8080092