Submitted:
23 July 2026
Posted:
24 July 2026
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Abstract
Keywords:
1. Introduction
2. Background

3. Materials and Methods
3.1. Sample Collection and Preparation Procedure
3.2. Proximate Analysis
3.3. Ultimate Analysis
3.4. Calorific Value Determination
3.5. Inorganic Element Analysis
4. Results and Discussion
4.1. Proximate Composition
4.2. Elemental Composition
4.3. Calorific Value
4.4. Inorganic Element Composition
4.5. Implications for Supercapacitor Electrode Fabrication
4.6. Comparative Assessment with Other Biomass Feedstocks

4.7. Optimisation Considerations for Biochar Production
5. Conclusions
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
Abbreviations
| BC | Biochar |
| C | Carbon |
| EDLC | Electrochemical Double Layer Capacitor |
| FC | Fixed Carbon |
| H | Hydrogen |
| N | Nitrogen |
| O | Oxygen |
| PL | Poultry Litter |
| S | Sulphur |
| VM | Volatile Matter |
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| Parameter | Content (weight %, dry basis) |
|---|---|
| Moisture Content | 4.89 |
| Volatile Matter | 70.26 |
| Ash Content | 6.34 |
| Fixed Carbon | 18.51 |
| Element | Content (weight %, dry ash-free basis) |
|---|---|
| Nitrogen | 2.11 |
| Carbon | 43.06 |
| Hydrogen | 6.13 |
| Sulphur | 1.68 |
| Oxygen | 40.68 |
| Parameter | Value (MJ kg⁻¹) |
|---|---|
| Higher heating value | 16.86 |
| Lower Heating Value | 15.32 |
| Element | Content (%) | Element | Content (%) |
|---|---|---|---|
| Silicon | 0.89 | Calcium | 4.12 |
| Phosphorus | 0.72 | Aluminium | 1.06 |
| Sulphur | 0.41 | Iron | 1.23 |
| Chlorine | 0.82 | Chromium | 0.09 |
| Potassium | 3.42 | Manganese | 0.24 |
| Copper | 0.11 | Zinc | 0.04 |
| Characteristic | Measured Value (%) | Implications for Electrodes | References |
|---|---|---|---|
| Carbon Content & Volatile Matter | C: 43.06 VM: 70.26 |
Provides sufficient precursor for porous carbon. High VM is released during pyrolysis and thus creates initial porosity that can be further developed by activation. | [44] |
| Fixed Carbon | 18.51 | Suggests a need for optimised activation (KOH, steam) to achieve the high surface areas (>1000 m²/g) required for high performance EDLCs. | [9] |
| Heteroatom Content (N, S) | N: 2.11 S: 1.68 |
Offers potential for self-doping. N- and S-containing functional groups can introduce pseudocapacitance, enhance conductivity, and improve electrode wettability, thereby boosting overall capacitance. | [6] |
| Inorganic Content (K, Ca) | K: 3.42 Ca: 4.12 |
Inherent K can act as a natural activation catalyst, thus potentially reducing the amount of external chemical activators needed. This can lower costs and simplify processing time. | [7] |
| Ash Content | 6.34 | Requires management. High ash can block micropores and increase electrode resistance. Demineralisation (acid washing) is likely necessary as a pre- or post-treatment step to curb the blockage occurrences. | [20] |
| Parameter | PL(%) | Switchgrass(%) [6] |
Sorghum(%) [6] |
Red Cedar(%) [6] |
|---|---|---|---|---|
| Nitrogen | 2.11 | 0.57 | 0.51 | 0.37 |
| Sulphur | 1.68 | 0.30 | 0.20 | 1.07 |
| VM | 70.26 | 70.36 | 68.10 | 71.79 |
| Ash | 6.34 | 4.62 | 5.05 | 4.09 |
| FC | 18.51 | 15.02 | 17.46 | 15.62 |
| Process Parameter | Optimisation Goal | Justification | References |
|---|---|---|---|
| Pyrolysis Temperature |
Moderate (400-600°C): For heteroatom retention. High (700-900°C): For high conductivity and graphitisation. |
Lower temperatures preserve beneficial N/S functional groups (pseudocapacitance), while higher temperatures improve electrical conductivity and carbon ordering but can eliminate heteroatoms. | [50] |
| Activation Strategy |
Chemical (KOH/NaOH): For ultra-high surface area. Physical (Steam/ CO₂): For a greener, simpler process. |
High surface area is paramount for EDLCs. KOH activation is highly effective but corrosive. The inherent K in the ash may allow for a reduced chemical-to-precursor ratio. | [51,52] |
| Demineralisation | Effective (Acid Washing): Target ash < 2-3% | Essential to prevent pore blockage by residual inorganics, which would otherwise reduce the active surface area and increase the internal resistance (IR drop) of the final electrode. | [19,53] |
| Heteroatom Retention |
Controlled atmosphere and Ramp rate: Maximise N/S functionality. Post-treatment: NH₃ or H₂S atmospheres. |
To fully exploit the self-doping advantage, pyrolysis conditions must be mild enough to retain heteroatoms. Post-treatment can further enrich surface chemistry. | [54] |
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