3.1.1. Montmorillonites
Polyester fabrics: as far as montmorillonites are considered, sodium cloisite (CNa) appears to be responsible for a significant TTI increase (192
vs. 160 s, respectively for PET + CNa
vs. PET,
Table 4) and respective EHC reduction (17.5
vs. 21.8 MJ/kg) for polyester with a consequent decrease of the burning kinetics in terms of pkHRR (80
vs. 90 kW/m
2) [
21] (and FPI). These parameters are plotted in
Figure 1, where, in addition, the effect of the other nanoparticles is described.
This finding suggests that PET combustion mechanism is partially changed; indeed, the nanoclay acting as an insulating physical barrier somehow protects polyester from heat and oxygen during combustion; therefore, the ignition time is delayed and effective heat is reduced (a lower amount of polymer burns) (
Figure 1). Furthermore, the presence of such clay on fabric surface causes a slight decrease of the TSR (87
vs. 90 m
2/m
2) and of their optical density (531
vs. 610 m
2/kg, SEA) as well as the CO and CO
2 yields.
Figure 1.
TTI, EHC and pkHRR values for nanoparticle-treated PET (area density = 171 g/m2).
Figure 1.
TTI, EHC and pkHRR values for nanoparticle-treated PET (area density = 171 g/m2).
Table 1.
Nanoparticles reviewed in this paper.
Table 1.
Nanoparticles reviewed in this paper.
Code | Family | Nanoparticle | Chemical formula | Modifier | Producer |
---|
Lamellar nanoparticles | | | | |
CNa | Montmorillonite | Sodium cloisite | Mx[Al4−xMgx](Si)8O20(OH)4 | - | Southern Clay Products, Inc. (Gonzales, TX, USA) |
HT | Hydrotalcite | Carbonate hydrotalcite | Mg6Al2(CO3)(OH16)·4(H2O) | Carbonate salt | Sasol Germany Gmbh (Hamburg, Germany) |
OS1 | Bohemite | Sulfonate bohemite | AlO(OH) | p-Toluenesulfonate salt | Sasol Germany Gmbh (Hamburg, Germany) |
Globular nanoparticles | | | | |
TiO2 | Titania (anatase crystalline form) | Titania | TiO2 | - | Huntsman International LLC (Varese, Italy) |
SiO2 | Silica | Silica | SiO2 | - | Elkem SA (Dusseldorf, Germany) |
POSS | Polyhedral oligomeric silsesquioxane | Octapropylammonium POSS® | R(SiOx) | - | Hybrid Plastics, Inc. (Hattiesburg, MS, USA) |
Table 2.
Dispersing agents.
Table 4.
Combustion data of untreated and nanoparticle-treated PET (d = 171 g/m2) by cone calorimetry.
Table 4.
Combustion data of untreated and nanoparticle-treated PET (d = 171 g/m2) by cone calorimetry.
Sample | TTI (s) | THR (MJ/m2) | EHC (MJ/kg) | pkHRR (kW/m2) | FPI (sm2/kW) | TSR (m2/m2) | SEA (m2/kg) | [CO] yield (kg/kg) | [CO2] yield (kg/kg) |
---|
PET | 160 ± 4 | 2.5 ± 0.6 | 21.8 ± 7.8 | 90 ± 9 | 1.89 ± 0.05 | 90 ± 8 | 610 ± 13 | 0.0486 ± 0.0228 | 3.85 ± 1.68 |
Lamellar nanoparticles | | |
PET + CNaa | 192 ± 7 | 2.8 ± 0.4 | 17.5 ± 2.5 | 80 ± 2 | 2.35 ± 0.04 | 87 ± 3 | 531± 41 | 0.0409 ± 0.0008 | 3.22 ± 0.14 |
PET + B500 + CNa (B500:CNa = 1:4) | 90 ± 6 | 2.5 ± 0.1 | 18.4 ± 2.0 | 74 ± 8 | 1.22 ± 0.09 | 80 ± 6 | 514 ± 70 | 0.0316 ± 0.0049 | 2.17 ± 0.03 |
PET + B500 + CNa (B500:CNa = 1:2) | 78 ± 10 | 2.5 ± 0.2 | 17.3 ± 1.8 | 78 ± 10 | 0.99 ± 0.13 | 78 ± 3 | 511 ± 34 | 0.0305 ± 0.0053 | 2.03 ± 0.24 |
PET + B500 + CNa (B500:CNa = 1:1) | 73 ± 12 | 2.3 ± 0.1 | 17.1 ± 1.6 | 63 ± 2 | 1.24 ± 0.09 | 72 ± 2 | 476 ± 34 | 0.0277 ± 0.0043 | 2.24 ± 0.31 |
PET + HTb | 226 ± 4 | 2.5 ± 0.9 | 16.4 ± 1.5 | 76 ± 7 | 2.97 ± 0.05 | 82 ± 7 | 358 ± 11 | 0.0261 ± 0.0011 | 2.43 ± 0.07 |
PET + PES + HT (PES:HT = 1:1) | 244 ± 9 | 2.3 ± 0.1 | 14.0 ± 3.1 | 56 ± 2 | 4.36 ± 0.04 | 89 ± 4 | 369 ± 36 | 0.0227 ± 0.0008 | 2.45 ± 0.19 |
PET + OS1 | 120 ± 6 | 2.4 ± 0.2 | 15.0 ± 0.9 | 70 ± 6 | 1.50 ± 0.06 | 76 ± 2 | 394 ± 14 | 0.0301 ± 0.0014 | 2.73 ± 0.06 |
PET + PES + OS1 (PES:OS1 = 1:1) | 258 ± 4 | 2.3 ± 0 | 23.0 ± 4.4 | 87 ± 7 | 2.97 ± 0.05 | 112 ± 9 | 554 ± 80 | 0.0305 ± 0.0046 | 3.34 ± 0.60 |
Globular nanoparticles | | | | | | | | | |
PET + TiO2b | 152 ± 6 | 2.3 ± 0.5 | 19.4 ± 5.0 | 70 ± 1 | 2.17 ± 0.33 | 76 ± 0 | 586 ± 17 | 0.0421 ± 0.0170 | 3.58 ± 1.19 |
PET + SiO2b | 105 ± 9 | 2.7 ± 0.1 | 16.0 ± 0.2 | 81 ± 11 | 1.30 ± 0.11 | 85 ± 0 | 477 ± 11 | 0.0302 ± 0.0006 | 2.71 ± 0.12 |
PET + POSS | 130 ± 9 | 2.4 ± 0 | 20.0 ± 6.3 | 66 ± 3 | 1.97 ± 0.06 | 91 ± 0 | 620 ± 17 | 0.0415 ± 0.0158 | 3.04 ± 0.93 |
Lamellar + globular nanoparticles | | | | | | | | | |
PET + HT + SiO2 (30 + 30 min) b | 240 ± 8 | 3.1 ± 0.9 | 17.02 ± 2.0 | 85 ± 8 | 2.82 ± 0.06 | 95 ± 5 | 512 ± 25 | 0.0123 ± 0.0006 | 2.81 ± 0.14 |
PET + HT + SiO2 (60 + 60 min) b | 294 ± 9 | 2.8 ± 0.7 | 23.18 ± 2.0 | 87 ± 9 | 3.38 ± 0.07 | 92 ± 5 | 558 ± 28 | 0.0130 ± 0.0006 | 3.54 ± 0.18 |
Table 5.
Combustion data of untreated and nanoparticle-treated PET (d = 490 g/m2) by cone calorimetry.
Table 5.
Combustion data of untreated and nanoparticle-treated PET (d = 490 g/m2) by cone calorimetry.
Sample | TTI (s) | THR (MJ/m2) | EHC (MJ/kg) | pkHRR (kW/m2) | FPI (sm2/kW) | TSR (m2/m2) | SEA (m2/kg) | [CO] Yield (kg/kg) | [CO2] Yield (kg/kg) |
---|
PET | 106 ± 20 | 6.7 ± 0.1 | 15.5 ± 0.1 | 210 ± 16 | 0.50 ± 0.14 | 227 ± 12 | 450 ± 41 | 0.0483 ± 0.0021 | 2.91 ± 0.01 |
Lamellar nanoparticles | | | | |
PET + CNa | 107 ± 7 | 6.8 ± 0.1 | 17.4 ± 1.6 | 237 ± 25 | 0.62 ± 0.06 | 226 ± 4 | 501± 78 | 0.0415 ± 0.0023 | 2.56 ± 0.31 |
PET + HT | 148 ± 2 | 6.5 ± 0.1 | 16.7 ± 0.1 | 233 ± 5 | 0.64 ± 0.02 | 198 ± 0 | 416 ± 19 | 0.0383 ± 0.0026 | 2.50 ± 0.08 |
PET + PES + HT (PES:HT = 1:1) | 112 ± 4 | 6.2 ± 0.1 | 16.4 ± 0.3 | 208 ± 6 | 0.54 ± 0.03 | 171 ± 2 | 363 ± 4 | 0.0311 ± 0.0019 | 2.41 ± 0.01 |
PET + NSI + HT (NSI:HT = 1:1) | 143 ± 3 | 6.1 ± 0.1 | 17.7 ± 1.9 | 226 ± 8 | 0.63 ± 0.03 | 191 ± 14 | 424 ± 29 | 0.0484 ± 0.0045 | 2.73 ± 0.24 |
PET + WP + HT (WP:HT = 1:1) | 124 ± 9 | 6.9 ± 0.4 | 17.7 ± 0.9 | 183 ± 18 | 0.68 ± 0.09 | 193 ± 11 | 398 ± 13 | 0.0436 ± 0.0047 | 2.55 ± 0.06 |
Globular nanoparticles | | | | | | | | | |
PET + SiO2 | 108 ± 2 | 7.1 ± 0.2 | 16.3 ± 0.7 | 215 ± 8 | 0.50 ± 0.03 | 243 ± 8 | 525 ± 13 | 0.0369 ± 0.0003 | 2.10 ± 0.05 |
PET + NSI + SiO2 (NSI:SiO2 = 1:1) | 119 ± 6 | 6.6 ± 0.2 | 16.4 ± 0.7 | 195 ± 18 | 0.61 ± 0.07 | 228 ± 8 | 493 ± 33 | 0.0397 ± 0.0012 | 2.50 ± 0.11 |
PET + WP + SiO2 (WP:SiO2 = 1:1) | 148 ± 1 | 6.6 ± 0.1 | 16.9 ± 1.2 | 244 ± 1 | 0.61 ± 0.01 | 230 ± 0 | 466 ± 18 | 0.0460 ± 0.0042 | 2.47 ± 0.11 |
Table 6.
Combustion data of untreated and nanoparticle-treated cotton (d = 210 g/m2) by cone calorimetry.
Table 6.
Combustion data of untreated and nanoparticle-treated cotton (d = 210 g/m2) by cone calorimetry.
Sample | TTI (s) | THR (MJ/m2) | EHC (MJ/kg) | pkHRR (kW/m2) | FPI (sm2/kW) | TSR (m2/m2) | SEA (m2/kg) | [CO] Yield (kg/kg) | [CO2] Yield (kg/kg) |
---|
Cotton | 14 ± 1 | 2.8 ± 0 | 17.0 ± 0.9 | 124 ± 6 | 0.11 ± 0.06 | 21 ± 2 | 25 ± 5 | 0.039 ± 0.0042 | 2.79 ± 0.18 |
Lamellar nanoparticles | | |
Cotton + CNa | 38 ± 3 | 2.5 ± 0.3 | 18.0 ± 5.4 | 85 ± 12 | 0.45 ± 0.11 | 36 ± 10 | 16 ± 7 | 0.0613 ± 0.0159 | 2.68 ± 0.88 |
Cotton + B500 + CNa (B500:CNa = 1:4) | 19 ± 2 | 2.8 ± 0.2 | 14.6 ± 0.6 | 87 ± 3 | 0.22 ± 0.07 | 16 ± 2 | 17 ± 2 | 0.0416 ± 0.0020 | 2.48 ± 0.06 |
Cotton + B500 + CNa (B500:CNa = 1:2) | 22 ± 6 | 2.5 ± 0.3 | 14.2 ± 6.5 | 79 ± 5 | 0.28 ± 0.17 | 18 ± 7 | 27 ± 3 | 0.0719 ± 0.0420 | 3.29 ± 1.17 |
Cotton + B500 + CNa (B500:CNa = 1:1) | 18 ± 9 | 2.4 ± 0.3 | 14.8 ± 2.1 | 60 ± 15 | 0.30 ± 0.38 | 16 ± 7 | 28 ± 3 | 0.0499 ± 0.0303 | 2.40 ± 0.23 |
Cotton + NSI + CNa (NSI:CNa = 1:1) | 22 ± 10 | 3.1 ± 0.1 | 15.1 ± 1.5 | 80 ± 3 | 0.14 ± 0.05 | 30 ± 4 | 92 ± 4 | 0.0198 ± 0.0027 | 2.30 ± 0.05 |
Cotton + C + CNa (1%) | 40 ± 1 | 2.4 ± 0.1 | 15.9 ± 0.5 | 97 ± 9 | 0.41 ± 0.06 | 28 ± 3 | 12 ± 6 | 0.0675 ± 0.0022 | 2.55 ± 0.11 |
Cotton + D + CNa (1%) | 24 ± 3 | 2.8 ± 0.2 | 20.6 ± 0.5 | 97 ± 3 | 0.25 ± 0.08 | 22 ± 3 | 7 ± 2 | 0.0445 ± 0.0025 | 3.09 ± 0.10 |
Cotton + E + CNa (1%) | 40 ± 2 | 2.1 ± 0.2 | 15.7 ± 6.5 | 77 ± 1 | 0.52 ± 0.03 | 46 ± 1 | 16 ± 2 | 0.0943 ± 0.0303 | 2.42 ± 0.72 |
Cotton + C + CNa (2%) | 19 ± 3 | 2.6 ± 0 | 14.9 ± 2.9 | 96 ± 1 | 0.20 ± 0.08 | 16 ± 1 | 12 ± 3 | 0.0464 ± 0.0027 | 2.38 ± 0.30 |
Cotton + D + CNa (2%) | 24 ± 8 | 2.7 ± 0.4 | 17.0 ± 3.1 | 95 ± 3 | 0.25 ± 0.18 | 22 ± 8 | 14 ± 7 | 0.0512 ± 0.0148 | 2.64 ± 0.45 |
Cotton + E + CNa (2%) | 36 ± 3 | 2.4 ± 0.1 | 18.4 ± 4.4 | 92 ± 6 | 0.39 ± 0.07 | 7 ± 3 | 10 ± 7 | 0.0637 ± 0.0267 | 2.81 ± 0.59 |
Cotton + C + CNa (5%) | 20 ± 4 | 2.8 ± 0.2 | 14.8 ± 1.8 | 94 ± 7 | 0.13 ± 0.02 | 22 ± 3 | 12 ± 4 | 0.0472 ± 0.0034 | 2.43 ± 0.24 |
Cotton + D + CNa (5%) | 32 ± 4 | 2.4 ± 0.2 | 14.6 ± 1.5 | 91 ± 11 | 0.35 ± 0.12 | 14 ± 8 | 12 ± 7 | 0.0575 ± 0.0122 | 2.41 ± 0.33 |
Cotton + E + CNa (5%) | 22 ± 4 | 2.7 ± 0.2 | 14.7 ± 1.5 | 97 ± 7 | 0.23 ± 0.13 | 9 ± 2 | 6± 2 | 0.0578 ± 0.0061 | 2.36 ± 0.18 |
Globular nanoparticles | | | | | | | | | |
Cotton + POSS b | 18 ± 3 | 2.2 ± 0.1 | 15.3 ± 3.5 | 76 ± 2 | 0.24 ± 0.10 | 9 ± 3 | 16 ± 3 | 0.0697 ± 0.0169 | 2.27 ± 0.55 |
Cotton + C + POSS (1%)b | 34 ± 1 | 2.2 ± 0.1 | 14.8 ± 1.0 | 85 ± 4 | 0.40 ± 0.04 | 35 ± 1 | 16 ± 4 | 0.0761 ± 0.0106 | 2.18 ± 0.04 |
Cotton + D + POSS (1%)b | 20 ± 5 | 2.4 ± 0.1 | 14.0 ± 0.6 | 84 ± 4 | 0.24 ± 0.15 | 17 ± 9 | 16 ± 4 | 0.0595 ± 0.0112 | 2.25 ± 0.09 |
Cotton + E + POSS (1%)b | 30 ± 2 | 2.3 ± 0 | 15.9 ± 1.7 | 93 ± 6 | 0.32 ± 0.07 | 27 ± 0 | 27 ± 7 | 0.0762 ± 0.0051 | 2.62 ± 0.28 |
Cotton + C + POSS (2%)b | 30 ± 4 | 1.7 ± 0.2 | 13.8 ± 0.9 | 58 ± 9 | 0.52 ± 0.14 | 57 ± 14 | 15 ± 3 | 0.1417 ± 0.0298 | 2.54 ± 0.19 |
Cotton + D + POSS (2%)b | 34 ± 4 | 1.5 ± 0.1 | 12.3 ± 1.3 | 52 ± 5 | 0.65 ± 0.11 | 57 ± 7 | 15 ± 3 | 0.1486 ± 0.0351 | 2.49 ± 0.24 |
Cotton + E + POSS (2%)b | 36 ± 2 | 1.8 ± 0.2 | 14.3 ± 1.1 | 67 ± 6 | 0.54 ± 0.07 | 42 ± 12 | 14 ± 2 | 0.1302 ± 0.0199 | 2.73 ± 0.17 |
Cotton + C + POSS (5%)b | 26 ± 2 | 1.9 ± 0.1 | 13.2 ± 0.3 | 62 ± 4 | 0.42 ± 0.07 | 27 ± 1 | 15 ± 3 | 0.0805 ± 0.0063 | 2.28 ± 0.17 |
Cotton + D + POSS (5%)b | 30 ± 7 | 1.3 ± 0.3 | 13.9 ± 1.6 | 44 ± 9 | 0.68 ± 0.22 | 39 ± 14 | 20 ± 4 | 0.1150 ± 0.0323 | 2.54 ± 0.16 |
Cotton + E + POSS (5%)b | 28 ± 3 | 2.1 ± 0.3 | 13.9 ± 1.6 | 67 ± 7 | 0.42 ± 0.11 | 23 ± 6 | 26 ± 4 | 0.0713 ± 0.0140 | 2.41 ± 0.14 |
Lamellar + globular nanoparticles | | | | | | | | | |
Cotton + C + CNa (1%) + POSS (1%) | 30 ± 2 | 2.3 ± 0.1 | 20.0 ± 5.1 | 90 ± 6 | 0.33 ± 0.07 | 27 ± 3 | 15 ± 6 | 0.0875 ± 0.0168 | 3.18 ± 0.83 |
Cotton + D + CNa (1%) + POSS (1%) | 21 ± 0 | 2.5 ± 0.1 | 13.1 ± 0.6 | 102 ± 4 | 0.21 ± 0.02 | 13 ± 2 | 20 ± 0 | 0.0486 ± 0.0096 | 1.83 ± 0 |
Cotton + E + CNa (1%) + POSS (1%) | 22 ± 5 | 2.4 ± 0.3 | 13.0 ± 2.6 | 84 ± 14 | 0.26 ± 0.20 | 18 ± 10 | 18 ± 2 | 0.0539 ± 0.0143 | 1.76 ± 0.34 |
Cotton + C + CNa (2.5%) + POSS (2.5%) | 20 ± 1 | 2.2 ± 0.1 | 14.4 ± 0.4 | 93 ± 7 | 0.22 ± 0.06 | 15 ± 5 | 14 ± 3 | 0.0699 ± 0.0002 | 2.40 ± 0.04 |
Cotton + D + CNa (2.5%) + POSS (2.5%) | 20 ± 6 | 2.0 ± 0.1 | 12.6 ± 0.4 | 70 ± 5 | 0.29 ± 0.19 | 25 ± 6 | 17± 8 | 0.0759 ± 0.0064 | 2.11 ± 0.09 |
Cotton + E + CNa (2.5%) + POSS (2.5%) | 26 ± 5 | 2.0 ± 0.1 | 13.3 ± 1.1 | 70 ± 9 | 0.37 ± 0.16 | 30 ± 8 | 19 ± 8 | 0.0939 ± 0.0266 | 2.28 ± 0.13 |
Cotton + HT + SiO2 (30 + 30 min) a | 30 ± 5 | 2.9 ± 0.3 | 2.9 ± 0.3 | 93 ± 8 | 0.32 ± 0.13 | 18 ± 10 | 11 ± 7 | 0.0254 ± 0.0067 | 2.08 ± 0.53 |
Cotton + HT + SiO2 (60 + 60 min) a | 37 ± 4 | 2.6 ± 0.1 | 2.6 ± 0.1 | 86 ± 4 | 0.43 ± 0.08 | 22 ± 7 | 9 ± 5 | 0.0291 ± 0.0053 | 2.14 ± 0.07 |
In order to further increase PET−CNa interactions, a pre-treatment of the fabric by cold oxygen plasma (
etching) was undertaken with different conditions of power and time (
Table 7), as already demonstrated by our group in a previous paper [
21]. In this case, no dispersing agent was employed to further increase the amount of nanoparticles in aqueous suspension.
The results collected by cone calorimetry and scanning electron microscopy (magnifications in ref. [
21]) show how the plasma pre-treatment can increase both clay surface density and the interactions between inorganic nanoparticles and PET surface. The best sample (PET+CNa_5) has exhibited an increase in time to ignition up to 104% and a reduction in the heat release rate of 10%.
Table 7.
Combustion data of PET (
d = 171 g/m
2) treated with sodium cloisite and plasma treatment by cone calorimetry [
21].
Table 7.
Combustion data of PET (d = 171 g/m2) treated with sodium cloisite and plasma treatment by cone calorimetry [21].
Sample | Plasma Power (w) | Plasma Time (s) | TTI (s) | THR (MJ/m2) | pkHRR (kW/m2) | FPI (sm2/kW) |
---|
PET | - | - | 158 ± 4 | 2.5 ± 0.4 | 90 ± 9 | 1.76 ± 0.06 |
PET + Can a | - | - | 198 ± 8 | 2.8 ± 0.4 | 105 ± 2 | 1.89 ± 0.03 |
PET + CNa_1 a | 120 | 15 | 244 ± 24 | 2.4 ± 0.4 | 85 ± 7 | 2.87 ± 0.08 |
PET + CNa_2 a | 120 | 60 | 261 ± 10 | 2.6 ± 0.1 | 89 ± 7 | 2.93 ± 0.03 |
PET + CNa_3 a | 120 | 80 | 192 ± 34 | 2.3 ± 0.4 | 94 ± 12 | 2.04 ± 0.15 |
PET + CNa_4 a | 50 | 180 | 241 ± 10 | 2.2 ± 0.8 | 92 ± 19 | 2.62 ± 0.07 |
PET + CNa_5 a | 80 | 180 | 322 ± 29 | 1.8 ± 0.4 | 81 ± 18 | 3.98 ± 0.16 |
In the opinion of the authors, the highest risk connected with the proposed approach of nanoparticle adsorption (namely, simple impregnation) can be the low swelling factor of the nanoclay within the aqueous medium; in this manner, a low amount of nanoparticles could be deposited on the fabric surface. For this reason, in the present study, the use of dispersing agents has been taken into account in order to increase the dispersion level of available sodium cloisite. To this aim, a sodium polyacrylate binding agent (B500,
Table 2), commonly used in industrial fabric finishing, was employed in different concentrations (B500: CNa = 1:4, 1:2 and 1:1, respectively) and the behavior of so-treated fabrics have been investigated (
Table 4). The presence of this species strongly influences PET TTI values such that they decrease (90, 78, and 73 s
vs. 160 and 192 s for neat PET or PET + CNa) (
Figure 1). A possible explanation can be related to the low thermal stability of the employed polyacrylate. Upon exposure to the cone heat flux, the early degradation of the polyacrylate could lead to the production of an overall increased amount of combustible volatiles, thus sensitizing the ignition of the sample. In spite of these results, it is possible to observe a significant reduction of (i) the combustion kinetics parameters in terms of pkHRR (
Figure 1); (ii) smoke generation (TSR and SEA) and (iii) CO and CO
2 yields as compared with the treatment with sodium cloisite alone. It is likely that a higher amount of nanoparticles have been deposited on the fabric surface, creating a more efficient physical barrier during PET combustion. However, from an overall consideration, assessing the FPI values for these systems, it is possible to conclude that the use of the B500 dispersing agent in combination with the CNa does not improve the flame-retardant properties of cotton as well as when only sodium cloisite is present (
Table 4).
Table 8.
Combustion data of untreated and nanoparticle-treated PET-cotton = 85:15 (d = 280 g/m2) blends by cone calorimetry.
Table 8.
Combustion data of untreated and nanoparticle-treated PET-cotton = 85:15 (d = 280 g/m2) blends by cone calorimetry.
Sample | TTI (s) | THR (MJ/m2) | EHC (MJ/kg) | pkHRR (kW/m2) | FPI (sm2/kW) | TSR (m2/m2) | SEA (m2/kg) | [CO] Yield (kg/kg) | [CO2] Yield (kg/kg) |
---|
PET−cotton (PET:cotton = 85:15) | 35 ± 5 | 3.7 ± 0.1 | 15.3 ± 0.4 | 150 ± 1 | 0.24 ± 0.07 | 107 ± 2 | 407 ± 6 | 0.0380 ± 0 | 2.94 ± 0.03 |
Lamellar nanoparticles | | |
PET−cotton 85:15 + CNa | 52 ± 5 | 3.6 ± 0.6 | 15.8 ± 3.4 | 107 ± 13 | 0.49 ± 0.19 | 122 ± 7 | 460 ± 26 | 0.0370 ± 0.0034 | 2.62 ± 0.20 |
Globular nanoparticles | | | | | | | | | |
PET−cotton 85:15 + SiO2 (30 min) | 26 ± 3 | 4.2 ± 0.1 | 16.4 ± 0.2 | 131 ± 8 | 0.20 ± 0.09 | 109 ± 4 | 417 ± 13 | 0.0264 ± 0.0009 | 2.43 ± 0.03 |
PET−cotton 85:15 + SiO2 (60 min) | 56 ± 7 | 3.9 ± 0.3 | 16.2 ± 0.5 | 128 ± 8 | 0.44 ± 0.09 | 118 ± 6 | 435 ± 34 | 0.0316 ± 0.0015 | 2.55 ± 0.07 |
Table 9.
Combustion data of untreated and nanoparticle-treated PET-cotton = 65:35 blend (d = 245 g/m2) by cone calorimetry.
Table 9.
Combustion data of untreated and nanoparticle-treated PET-cotton = 65:35 blend (d = 245 g/m2) by cone calorimetry.
Sample | TTI (s) | THR (MJ/m2) | EHC (MJ/kg) | pkHRR (kW/m2) | FPI (sm2/kW) | TSR (m2/m2) | SEA (m2/kg) | [CO] Yield (kg/kg) | [CO2] Yield (kg/kg) |
---|
PET−cotton (PET:cotton = 65:35) | 11 ± 1 | 3.4 ± 0.2 | 15.3 ± 0.3 | 140 ± 5 | 0.08 ± 0.06 | 53 ± 9 | 259 ± 12 | 0.0313 ± 0.0021 | 2.91 ± 0.03 |
Lamellar nanoparticles | | |
PET−cotton 65:35 + CNa | 24 ± 4 | 3.7 ± 0.1 | 17.1 ± 0.3 | 125 ± 7 | 0.19 ± 0.13 | 76 ± 1 | 329 ± 24 | 0.0328 ± 0.0049 | 2.54 ± 0.11 |
PET−cotton 65:35 + HT (30 min) | 74 ± 1 | 2.7 ± 0.3 | 15.2 ± 2.6 | 121 ± 1 | 0.61 ± 0.01 | 102 ± 2 | 315 ± 50 | 0.0304 ± 0.0023 | 2.71 ± 0.54 |
PET−cotton 65:35 + HT (60 min) | 20 ± 8 | 3.0 ± 0.2 | 16.3 ± 0.8 | 94 ± 6 | 0.21 ± 0.23 | 65 ± 9 | 302 ± 15 | 0.0219 ± 0.0015 | 2.71 ± 0.12 |
Globular nanoparticles | | | | | | | | | |
PET−cotton 65:35 + SiO2 (30 min) | 20 ± 1 | 3.6 ± 0.1 | 16.7 ± 1.3 | 130 ± 5 | 0.15 ± 0.04 | 65 ± 5 | 289 ± 23 | 0.0265 ± 0.0028 | 2.57 ± 0.21 |
PET−cotton 65:35 + SiO2 (60 min) | 20 ± 1 | 3.4 ± 0.1 | 23.2 ± 13.4 | 127 ± 2 | 0.16 ± 0.03 | 65 ± 3 | 266 ± 54 | 0.0365 ± 0.0214 | 2.44 ± 0.68 |
Lamellar + globular nanoparticles | | | | | | | | | |
PET−cotton + HT + SiO2 (30 + 30 min) | 54 ± 1 | 2.6 ± 0.3 | 16.5 ± 4.1 | 115 ± 4 | 0.47 ± 0.03 | 81 ± 1 | 337 ± 70 | 0.0281 ± 0.0041 | 2.69 ± 0.47 |
PET−cotton + HT + SiO2 (60 + 60 min) | 40 ± 2 | 3.4 ± 0.3 | 15.8 ± 2.0 | 105 ± 7 | 0.39 ± 0.08 | 58 ± 2 | 266 ± 38 | 0.0076 ± 0.0003 | 2.51 ± 0.41 |
The same nanoparticle has been tested using a PET fabric having a higher area density rather than of that previously used (490 g/m
2 vs. 171 g/m
2). The data collected in
Table 5 show that sodium cloisite is not effective in enhancing the flame retardancy of this heavier weight polyester. This can be ascribed to the denser structure of this fabric that inhibits nanoclay adsorption on PET surface. On the other hand, it is reasonable to conclude that doubling the area density will double the amount of fuel per unit area and that, if the level of clay is the same, it will be less efficient at reducing flammability.
Cotton: as far as cotton is concerned (
Table 6), sodium cloisite shows that is able to increase its TTI in a remarkable way (38 s
vs. 14 s for cotton + CNa and cotton, respectively), reducing pkHRR (87 kW/m
2 vs. 124 kW/m
2, a reduction of 30%) at the same time. The resulting FPI value is higher than that of pure cotton (0.45 sm
2/kW
vs. 0.11 sm
2/kW).
Also in this case, the B500 chemical has been employed as dispersing agent for improving sodium cloisite dispersion level; once again, a strong decrease of cotton TTI occurs (regardless of B500:CNa ratio), but also a significant decrease of pkHRR is observed in comparison with the pure fabric, as shown in
Figure 2. However, the highest reduction was assessed when the B500:CNa ratio was 1:1.
An alternative dispersing agent under study has been sodium polysulfonatenaphthalene (NSI,
Table 2). This species was assumed to be more promising than the sodium polyacrylate as it should not hydrolyze cotton and, in addition, naphthalene groups could promote cellulose carbonization, favoring a somewhat flame-retardant effect. In spite of these considerations, the performances of NSI-treated fabrics have not exhibited any improvements in terms of TTI, EHC and pkHRR (
Table 6) if compared with the fabric treated with only CNa (
Figure 2).
However, it is important to highlight that CNa (regardless of its amount) causes a substantial increase in total smokes and CO and CO2 yields.
Figure 2.
TTI, EHC and pkHRR values for cotton treated with CNa and B500 chemical.
Figure 2.
TTI, EHC and pkHRR values for cotton treated with CNa and B500 chemical.
An alternative approach to increasing the nanoparticle amount deposited on the cotton surface has been the use of a binder able to covalently link the hydroxyl groups on CNa surface to the hydroxyl group of C(6) glucose unit present in the cotton cellulose structure. With this aim, dicyanamide−formaldehyde polymer, melamine−formaldehyde and dimethylol(dihydroxy)ethyleneurea (C, D and E species in
Table 3) were employed to link different nominal amounts of sodium cloisite (namely, 1, 2 and 5 wt%). From the collected data (
Table 6), it is possible to conclude that all the chosen binders significantly affects cotton combustion, increasing TTI and decreasing pkHRR, regardless of nanoparticle amount. Also the smoke release has been reduced in the presence of these binders as compared with the cotton + CNa sample (TSR values).
Since sodium cloisite has shown some level of flame-retardant performances for both the polyester and cotton, two different blends of them were treated in a similar manner with the clay.
Table 8 and
Table 9 show that CNa is an efficient flame retardant for PET:cotton = 85:15 and PET:cotton = 65:35 blends since its presence increases their TTI (52 s
vs. 35 s and 11
vs. 24 s, respectively) and slightly decreases pkHRR (150 kW/m
2 vs. 107 kW/m
2 and 140 kW/m
2 vs. 125 kW/m
2, respectively), regardless of blend composition. However, once again, the presence of CNa causes a strong increase of smoke generation during combustion.
3.1.2. Hydrotalcites
As it is well known [
24], hydrotalcites are anionic nanoclays with a chemical formula of Mg
6Al
2(CO
3)(OH
16)·4(H
2O) (
Table 1). The high water content present in the structure of HT (hydrotalcite) can be responsible for a delay in TTI, as already demonstrated by our research group for both the polyester [
9] (
Figure 1) and cotton fabrics [
23]. Indeed, these nanoparticles are able to partially protect a polymer from the heat and oxygen as they form a ceramic layer during combustion, releasing a great amount of water upon heating. In this manner, the degradation products released by the polymer are diluted, causing a significant delay of ignition. This has been observed on both synthetic (namely, PET) and natural (cotton) fabrics. In detail, comparing the data collected in
Table 4, it is possible to observe that PET TTI increases from 166 up to 226 s and pkHRR decreases from 90 to 56 kW/m
2 thanks to the presence of adsorbed hydrotalcite (
Figure 1). The use of a binder-like PES (
Table 3) further promotes TTI increase (244 s and 226 s
vs. 160 s for PET + PES + HT, PET + HT and PET, respectively). In the meantime, these nanoparticles significantly affect also the combustion kinetics as shown by comparing respective sample EHC and pkHRR values in
Table 4 and plotted in
Figure 1. From an overall consideration, the highest FPI value registered is for the PET + PES + HT system in comparison with neat PET and the other lamellar-based systems under investigation (4.36 sm
2/kW
vs. 1.89 sm
2/kW,
Table 4).
The same increasing trend in TTI has been observed using the polyester with the higher area density (148 s
vs. 106 s for PET + HT and PET, respectively,
Table 5). The use of different dispersing agents, however, did not suggest their use as means to further increase this parameter.
Referring to cotton,
Table 10 reports the collected data of cotton treated with HT for two impregnation times (namely, 30 and 60 min): it is clear that this nanoparticle acts by the same way already observed for PET, by improving cotton TTI and significantly reducing pkHRR; as a consequence, the FPI value of HT-treated fabrics is higher than that of untreated cotton [
22]. Comparing the two samples obtained with different times, it is possible to note that a more prolonged immersion time does not increase the nanoparticle effect and probable amount, and thus the resulting flame-retardant properties.
Table 10.
Combustion data of untreated and hydrotalcite-treated cotton (
d = 210 g/m
2) by cone calorimetry [
22].
Table 10.
Combustion data of untreated and hydrotalcite-treated cotton (d = 210 g/m2) by cone calorimetry [22].
Sample | TTI (s) | pkHRR (kW/m2) | FPI (sm2/kW) |
---|
Cotton | 14 ± 1 | 124 ± 6 | 0.11 ± 0.02 |
Cotton + HT (30 min) | 34 ± 1 | 87 ± 1 | 0.39 ± 0.06 |
Cotton + HT (60 min) | 22 ± 5 | 94 ± 2 | 0.23 ± 0.03 |
As much as hydrotalcite has improved fire performance of polyester [
9] and cotton [
22], analogous experiments and results for PET:cotton = 65:35 blend show that the TTI increases from 11 to 74 s (
Table 9).
3.1.3. Bohemites
As far as bohemites are concerned, theoretically these nanoparticles have intrinsic flame-retardant features as they are aluminum oxide hydroxides, the γ-AlO(OH), that dehydrate in the range of 100–300 °C, releasing water and subsequently transforming into crystalline the γ-Al
2O
3 phase at
circa 420 °C [
25]. In doing so, during the first degradation step, the volatile products generated by polymers under irradiation are diluted and the ignition is reached after a longer time as compared with pure polymeric material. Furthermore, the ceramic barrier due to the presence of the just-formed alumina inhibits the further combustion.
Table 11 shows that p-toluenesulfonate salt bohemite (OS1) is able to delay cotton TTI (alone or covalently linked with some binders); furthermore, its pkHRR is significantly reduced, as are the production of smoke and CO and CO
2 yields [
23]. All formulations under investigations have exhibited a higher FPI value if compared with untreated cotton.
Table 11.
Combustion data of untreated and bohemite-treated cotton (
d = 210 g/m
2) by cone calorimetry [
23].
Table 11.
Combustion data of untreated and bohemite-treated cotton (d = 210 g/m2) by cone calorimetry [23].
Sample | TTI (s) | pkHHR (kW/m2g) | FPI (sm2g/kW) |
---|
Cotton | 14 ± 1.0 | 57 ± 6 | 0.24 ± 0.02 |
Cotton + OS1 | 22 ± 2.2 | 50 ± 5 | 0.44 ± 0.04 |
Cotton + A + OS1 | 22 ± 2.0 | 41 ± 4 | 0.54 ± 0.05 |
Cotton + B + OS1 | 20 ± 2.0 | 45 ± 4 | 0.44 ± 0.0 |
Cotton + C + OS1 | 20 ± 2.0 | 36 ± 3 | 0.56 ± 0.06 |
Cotton + D + OS1 | 21 ± 1.5 | 35 ± 5 | 0.60 ± 0.06 |
Cotton + E + OS1 | 20 ± 1.0 | 46 ± 4 | 0.43 ± 0.04 |
As far as polyester is concerned, bohemite alone does not affect its TTI; however, it reduces the EHC (15.0 MJ/kg
vs. 15.8 MJ/kg for PET + OS1 and PET, respectively,
Table 4), pkHRR (from 90 to 70 kW/m
2) (
Figure 1), TSR (from 90 to 76 m
2/m
2), SEA (from 610 to 394 m
2/kg) and CO and CO
2 yields. The use of a binder, such as PES, can be useful if the main goal is to increase the TTI (from 160 up to 258 s,
Table 4,
Figure 1), but it does not decrease the combustion kinetics; indeed, the pkHRR is nearly constant. As a consequence, PET + OS1 exhibited a lower FPI value with respect to PET while for PET + PES + OS1 the opposite trend was observed (
Table 4).