Thermal-treatment of KOH-soaked soybean |
1 M Na2SO4 aqueous solution |
1.8 V |
14.3 Wh kg−1
|
- |
[33] |
Hydrothermal treatment, KOH activation and then carbonization |
1 M Li2SO4 aqueous solution |
1.7 V |
18 Wh kg−1 (at 0.2 Ag−1) |
10,000 cycles: 90–95% retention |
[34] |
Hydrothermal treatment, KOH activation and then carbonization |
1 M Na2SO4 aqueous solution |
2.0 V |
22.28 Wh kg−1 (at 0.5 Ag−1) |
10,000 cycles: 91.1% retention at 5 Ag−1
|
[35] |
Hydrothermal and then carbonization |
1 M Na2SO4 aqueous solution |
1.9 V |
35 Wh kg−1 (at 0.1 Ag−1) |
2000 cycles: 81.4% retention at 0.5 Ag−1
|
[36] |
Hydrothermal treatment, carbonization and then KOH activation |
6 M KOH aqueous solution |
1.0 V |
36.11 Wh kg−1 (at 0.5 Ag−1) |
10,000 cycles: 87.5% retention at 10 Ag−1
|
[37] |
Hydrothermal treatment, KOH activation and then carbonization |
CMC–LiNO3 gel electrolyte |
2.0 V |
68.19 Wh kg−1 (at 1.0 Ag−1) |
5000 cycles: 89.9% retention at 2 Ag−1
|
This work |