ACP04
Material description
Material ID: ACP04
Material type: Predominantly organic composition rich in aromatics, such as cellulose-based and/or phenolic polymers.
Polymer: Cellulose and phenolic binder (100%)
Additives (fire retardants, fillers or traces of inorganic elements): Traces of other elements (<1%)
Core thickness: 2.76mm
Thickness of single metal skin: 0.51mm

| Compound | Mass Concentration (%) |
|---|---|
| Cellulose and phenolic binder (-) | 100 |
| Traces of calcium (Ca) | <1 |
| Traces of sodium (Na) | <1 |
| Traces of potassium (K) | <1 |
| Traces of sulfur (S) | <1 |
| Traces of silicon (Si) | <1 |
A. Material composition identification
A.1 Attenuated total reflection – Fourier transform infrared spectroscopy (ATR-FTIR)
Table 2. FTIR compound identification.| Identified Compounds |
|---|
| Cellulose and phenolic binder (-) |

Figure 1 . FTIR spectra: Absorbance percentage versus wavenumber from the sample.

Figure 2. FTIR spectra: Absorbance percentage versus wavenumber from the sample and the identified compounds.
A.2 Energy Dispersive X-Ray Fluorescence (EDXRF)
Table 2. Inorganic elements and their mass concentration identified with EDXRF.
| Element | Mass Concentration (%) |
|---|---|
| Ca | <1 |
| Na | <1 |
| K | <1 |
| S | <1 |
| Si | <1 |

Figure 3. EDXRF spectra. Counts vs energy. Identified elements are shown as vertical lines.
B. Thermogravimetric analysis
Table 3. Mass fraction of residue after thermal decomposition.
| Condition | Fraction of mass residue at 800°C |
|---|---|
| Non-oxidative (nitrogen) | 0.38 |
| Oxidative (air) | 0.03 |
Table 4. Temperature and amplitude of main peaks in non-oxidative conditions.
| Peak ID | Temperature peak (°C) | Amplitude of peak (°C-1) |
|---|---|---|
| Peak 1 | 343 | 5.58 x 10-3 |
| Peak 2 | 413 | 1.52 x 10-3 |
Table 5. Temperature and amplitude of main peaks in oxidative conditions.
| Peak ID | Temperature peak (°C) | Amplitude of peak (°C-1) |
|---|---|---|
| Peak 1 | 337 | 5.18 x 10-3 |
| Peak 2 | 451 | 7.65 x 10-3 |

Figure 4. Normalised mass (solid line) and derivative of the normalised mass (dashed line) in 150 ml min-1 of nitrogen and a heating rate of 20°C min-1.

Figure 5. Normalised mass (solid line) and derivative of the normalised mass (dashed line) in 150 ml min-1 of air and a heating rate of 20°C min-1 .
. Gross Heat of Combustion
Table 7. Gross Heat of Combustion individual results for sample.| Trial | ΔHc [kJ g-1] |
|---|---|
| Trial 1 | 22.72 |
| Trial 2 | 22.65 |
| Trial 3 | 23.01 |
| Average | 22.79 |
| Std dev | 0.19 |
D. Ignition parameters
Table 8. Summary of ignition parameters for sample.| Critical heat flux for ignition | Ignition temperature | Total heat transfer coefficient of losses | Apparent thermal inertia |
|---|---|---|---|
| q̇″cr [kW m−2] | Tig [°C] | hr [W m-2 K-1] | kρc [kW2 m-4 K-2 s] |
| 20.40 | 433 | 44.50 | 0.728 |

Figure 6. Time-to-ignition vs incident radiant heat flux for samples.
E. Burning behaviour
Table 9. Summary of key burning behaviour metrics.
| Heat flux | Test | Time to ignition | Fraction of mass residue | Peak heat release rate | Total energy released |
|---|---|---|---|---|---|
| q̇″inc [kW m-2] | tig [s] | mres [-] | q̇″p [kW m-2] | Qt [MJ m-2] | |
| 35 kW m-2 | |||||
| Test 1 | 78 | 0.09 | 173.50 | 52.10 | |
| Test 2 | 91 | 0.24 | 212.79 | 63.95 | |
| Avg | 84 | 0.17 | 193.15 | 58.02 | |
| 50 kW m-2 | |||||
| Test 1 | 39 | 0.04 | 243.59 | 58.37 | |
| Test 2 | 67 | 0.12 | 270.20 | 109.87 | |
| Avg | 53 | 0.08 | 256.90 | 84.12 | |
| 60 kW m-2 | |||||
| Test 1 | 33 | 0.02 | 237.45 | 64.70 | |
| Test 2 | - | - | - | - | |
| Avg | 33 | 0.02 | 237.45 | 64.70 | |
| 80 kW m-2 | |||||
| Test 1 | - | - | - | - | |
| Test 2 | - | - | - | - | |
| Avg | - | - | - | - |

Figure 7. Normalised mass loss over time for samples tested with 35, 50, 60 and 80 kW m-2.

Figure 8. Heat release rate per unit area over time for samples tested with 35, 50, 60 and 80 kW m-2.
| Test | ΔHc [kJ g-1] |
|---|---|
| 35 kW m-2 (Test 1) | 16.75 |
| 35 kW m-2 (Test 2) | 23.06 |
| 50 kW m-2 (Test 1) | 17.19 |
| 50 kW m-2 (Test 2) | 34.08 |
| 60 kW m-2 (Test 1) | 18.51 |
| 60 kW m-2 (Test 2) | - |
| 80 kW m-2 (Test 1) | - |
| 80 kW m-2 (Test 2) | - |
| Average | 21.92 |
| Std dev | 7.24 |
F. Flame Spread
Table 11. Minimum heat flux for flame spread rate and minimum flame spread rate for sample.| Orientation | q̇″min.spread [kW m-2] | Vf.min [mm s-1] |
|---|---|---|
| Horizontal | 10 | 0.40 |
| Vertical | 3 | 1.20 |

Figure 9. Lateral flame spread rate versus heat flux.

Figure 10. Vertical flame spread rate versus heat flux.

Figure 11. Vf-1/2 as function of q̇″ext in horizontal configuration.

Figure 12. Vf-1/2 as function of q̇″ext in vertical configuration.
Table 12. Flame spread parameter results for sample.
| Orientation | Trial | (kρcp⁄Φh2)1⁄2 [m3⁄2 s1⁄2 kW-1] | Φ [kW2 m-3] |
|---|---|---|---|
| Horizontal | 1 | 5.17 | 13.75 |
| Horizontal | 2 | 1.983 | 91.42 |
| Vertical | 1 | - | 1000 |
| Vertical | 2 | - | 1000 |