Ting Liuab,
Jian Jinga,
Yan Zhang
*b and
Zhengping Fangab
aMOE Key Laboratory of Macromolecular Synthesis and Functionalization, Department of Polymer Science and Engineering, Zhejiang University, Hangzhou, 310027, China
bLab of Polymer Materials and Engineering, Ningbo Institute of Technology, Zhejiang University, Ningbo, 315100, China. E-mail: hnpdszy@163.com
First published on 24th January 2018
To improve the flame resistance of PLA, a novel phosphorus-containing flame retardant (PFRS) was synthesized via the A2 + B3 type reaction of bisphenolic acid-based monomer (DPM, A2) and phosphorus oxychloride (POCl3, B3). Flame retardant PLA composite containing 15 wt% PFRS could achieve an LOI value of 24.3%, as well as a UL-94 V2 rating. Based on the structure of PFRS, here, intumescent flame retardant (IFR) systems were prepared by combining PFRS with ammonium polyphosphate (APP). The resultant PLA/PFRS/APP samples showed excellent fire-resistance properties such as self-extinguishing behavior and extremely low heat release rates. The LOI value of PLA composite with the addition of 3.8 wt% PFRS and 11.2 wt% APP could reach 29.7% and pass UL-94 V0 rating, and the PHRR value decreased by 46% compared to pure PLA. Investigation of the morphologies of the charred residues by Scanning Electron Microscopy (SEM) and Raman spectroscopy revealed the intrinsic charring ability of IFR systems to form a heat-protective intumescent-like barrier on the surface of PLA.
The approach of blending PLA resin with flame-retardant additives is regarded as the most effective way to prepare flame retardant PLA.14 Halogenated flame retardants are widely used for capturing free radicals and hence remove the capability of the flame propagation.15,16 However, halogenated additives tend to release a lot of smoke and toxic gases that are harmful to human health and environment.17,18 As we know, intumescent flame retardant (IFR) is considered as a promising halogen-free flame retardant due to its advantages of high efficiency, low toxicity, low smoke and no molten dropping during burning.19–23 However, traditional IFR additives exhibit low flame-retardant efficiency in PLA with only UL-94 V2 rating was achieved.24 In most cases, the hybrid IFR systems have improved flame-retardancy of polymer materials efficiently such as metal complexes/APP epoxy resins,25,26 hyperbranched char foaming agent/APP retarded PLA blends,27 and LDH/intumescent flame retarded PLA compounds.28 Chen29 et al. combined chitosan (CS) with APP to product flame-retardant PLA, and found that PLA composite containing 2% CS and 5% APP could reach LOI value of 33.1% and PHRR decrease to 425.6 kW m−2. Tang30 et al. reported that the co-addition of organo-modified sepiolite (OSEP) and IFR could significantly reduce the PHRR and THR values of PLA during combustion. All above mentioned ways have taken advantage of the synergistic effect among components to realize the development of high-effect green flame retardant systems.
Inspired by these works, a novel green polyphosphate flame retardant (PFRS) was synthesized by using diphenolic acid (DPA) as one of the raw materials. As is known, DPA is a potential platform chemical derived from biomass.31,32 Structure and properties of PFRS were well characterized by nuclear magnetic resonance (1H NMR, 13C NMR and 31P NMR), Fourier transform infrared (FTIR) and thermo gravimetric analysis (TGA). PFRS was deemed as acid source and carbon source in view of its unique structure. Therefore, IFR systems could be produced by combining PFRS with APP (acid source and gas source). The flame-retardant properties of PLA/PFRS and PLA/PFRS/APP systems were investigated in this study. Limiting oxygen index, vertical burning test, thermo gravimetric analysis and cone calorimetry tests were used to evaluate the thermostability and flame-retardant properties of various PLA composites. In addition, the morphology and structure of char residues were investigated by Scanning Electron Microscope (SEM) and Raman spectra. According to the data obtained, the flame retardant PLA composite was optimized and the mechanism was also clarified.
A mixture of 15.0 g DPM and 130 mL acetonitrile was added into a 250 mL completely-dried three-necked round bottom flask equipped with mechanical stirrer, reflux condenser and nitrogen inlet. The equipment was then cooled to 0 °C by an external ice-salt bath. When the reactants were dissolved completely, X mL (X = 3.68, 3.06, 2.14, 1.53, 0.92) POCl3 in 20 mL acetonitrile was added drop wise for about 1 h at 0–5 °C with constant stirring speed. In order to accelerate this acylation reaction, 9.3 mL TEA was added into the flask as absorb acid agent at intervals of an hour for three times. After that, the temperature was raised to 50 °C and continued for 2 h. Finally, the reaction kept for another 6 h under the temperature of 80 °C. After reaction finished, products in solution and precipitate were collected respectively at room temperature.
As for the products in solution, the solvent was evaporated by rotary evaporation at reduced pressure and the residue after evaporation was washed with hot deionized water for three times. These obtained solids were dried at 80 °C by a vacuum oven for 12 h.
As for the precipitate, the yield of precipitate appeared to change along with the mixture proportion of POCl3, which was analyzed with the method of Soxhlet extraction. According to the Soxhlet's procedure,34 the precipitate samples were dried in a vacuum oven at 80 °C for 12 h, then grounded into small particles and placed in a porous bag-type filter paper. Thereafter, the filter paper was placed in an extraction chamber, which was suspended above a flask containing the solvent acetonitrile. Then, a condenser was arranged on the extraction chamber. Finally, the equipment was heated to the reflux temperature and acetonitrile evaporated and moved up into the condenser, where it was converted into a liquid that trickled into the extraction chamber which loading with specimens. Extraction was continued for 12 h under this condition. After extraction, the residues were collected, dried completely and recorded the weight, these insoluble matters were identified as cross-linking products.
Sample | Composition (wt%) | ||
---|---|---|---|
PLA | PFRS | APP | |
PLA | 100 | 0 | 0 |
PLA/15PFRS | 85 | 15 | 0 |
PLA/7.5PFRS/7.5APP | 85 | 7.5 | 7.5 |
PLA/5PFRS/10APP | 85 | 5 | 10 |
PLA/3.8PFRS/11.2APP | 85 | 3.8 | 11.2 |
PLA/3PFRS/12APP | 85 | 3 | 12 |
PLA/15APP | 85 | 0 | 15 |
It is interested to find that the structure of products appeared to change along with the mixture proportion of reactant POCl3. In order to investigate the synthesis mechanism, a series of reactions with different DPM/POCl3 molar ratios were carried out. It can be found that the products would be precipitated off in the case of an excess addition of DPM such as nDPM:
nPOCl3 = 1
:
0.7. Conversely, when the addition of DPM was not excessive such as nDPM
:
nPOCl3 = 1
:
1.2 and 1
:
1, the reaction products mainly existed in solution. FTIR spectrum was used to analyse these products and the representative results were presented in Fig. 1. It was obvious that the absorption peak of –OH bond shifted to lower wave numbers with the increase addition of POCl3, which was due to the growing number of red-shift hydrogen bonds.36 Furthermore, the relative absorption intensity of the peak at 1289 cm−1 (–P
O) was enhanced along with increasing addition of POCl3, it was due to the increased content of POCl3 units.
![]() | ||
Fig. 1 FTIR spectra of the precipitate products with nDPM![]() ![]() ![]() ![]() ![]() ![]() ![]() ![]() ![]() ![]() |
When the addition of POCl3 was excessive, phosphate groups become the main end groups. Such structures could bring out products good solubility. Accordingly, the proportion of the insoluble matters was usually characterized by their degree of cross-linking (DC), which was determined here by using equation as follows:
DC = C/(B + C) × 100% |
B and C referred to the weight of soluble and cross-linking products in this reaction. Experimentally, DC was determined by Soxhlet's procedure as mentioned in part 2.2, and the results were presented in Fig. 2. The values of DC for the reaction were found to be smaller with increasing addition of POCl3, which was agreed with the FTIR spectra. On basis of the above results, it can be demonstrated that the synthesis pathway of this reaction as is shown in Scheme 1.
However, the cross-linking product was poor in processing performance due to the insolubility and infusibility. In consideration of the compatibility with PLA, only PFRS synthesized under reactants molar ratios DPM:
POCl3 = 1
:
1 was studied in this work.
The 13C NMR spectrum further supports the structure of PFRS as shown in Fig. 3(b). The peaks observed at 155.0 (C1), 114.7 (C2), 127.7 (C3), 139.1 (C4), 27.3 (C5), 36.9 (C6), 29.4 (C7), 43.7 (C8) ppm were assigned to the carbon atoms in the DPA subunit. The peak at δ = 172.7 ppm may be due to the carbon of ester carbonyl (C9). The peaks at 59.4 (C10), 36.0 (C11) and 75.5 (C12) ppm were attributed to the carbon atoms in caged PEPA subunit. See from Fig. 3(c), the higher peak at −7.55 ppm could be assigned to the phosphorus atoms in middle units and the lower peak at −7.05 ppm was correspond with the terminal group phosphorus atoms.
The TG and DTG curves of PFRS in nitrogen atmosphere are presented in Fig. 4. PFRS exhibited a three-steps decomposition in the temperature ranges of 50–180 °C, 250–400 °C, and 400–900 °C in accordance with water and small molecules like phosphoric falling off, the further carbonization and the thermal degradation of char residue, respectively.37 Besides, the residue of PFRS at 600, 700 and 800 °C was 42.1%, 41.0%, and 39.3%, respectively. It suggested the potential charring ability of PFRS.
Sample | LOI (%) | UL-94 rating | t1a (s) | t2b (s) | Dripping | Igniting cotton |
---|---|---|---|---|---|---|
a t1: the burning time after first ignition.b t2: the burning time after second ignition. | ||||||
PLA | 20.0 | Failed | — | — | Yes | Yes |
PLA/15PFRS | 24.3 | V2 | 10 | 9 | Yes | Yes |
PLA/7.5PFRS/7.5APP | 28.3 | V0 | 1 | 3 | Yes | No |
PLA/5PFRS/10APP | 28.8 | V0 | 1 | 1 | Yes | No |
PLA/3.8PFRS/11.2APP | 29.7 | V0 | 0 | 1 | Yes | No |
PLA/3PFRS/12APP | 28.6 | V0 | 0 | 1 | Yes | No |
PLA/15APP | 26.0 | V2 | 13 | 5 | Yes | Yes |
Cone calorimetry had been employed to investigate the dynamic combustion behaviors of PLA and PLA composites, which could provide various parameters such as time to ignition (TTI), peak heat release rate (PHRR), total heat release (THR) and residue mass (RM). HRR and THR curves of various PLA samples are illustrated in Fig. 5 and 6, and more detailed information from cone calorimetric test are listed in Table 3.
Sample | TTI (s) | PHRR (kW m−2) | THR (MJ m−2) | RM (%) | FIGRA (kW m−2 s−1) |
---|---|---|---|---|---|
PLA | 68 ± 1 | 419 ± 3 | 70.3 ± 0.1 | 1.6 ± 0.2 | 2.2 |
PLA/15PFRS | 52 ± 0 | 362 ± 13 | 61.5 ± 0.9 | 6.2 ± 0.7 | 2.2 |
PLA/7.5PFRS/7.5APP | 54 ± 1 | 257 ± 6 | 57.9 ± 3.4 | 11.5 ± 1.7 | 2.1 |
PLA/5PFRS/10APP | 56 ± 0 | 287 ± 8 | 57.0 ± 0.7 | 10.2 ± 0.5 | 1.7 |
PLA/3.8PFRS/11.2APP | 54 ± 2 | 227 ± 3 | 41.9 ± 0 | 22.6 ± 0 | 1.4 |
PLA/3PFRS/12APP | 57 ± 0 | 232 ± 5 | 52.0 ± 0.5 | 13.5 ± 0 | 1.5 |
PLA/15APP | 62 ± 0 | 239 ± 3 | 48.5 ± 0.5 | 19.4 ± 0.6 | 1.6 |
With the incorporation of 15 wt% PFRS into PLA, the TTI was shortened to 52 seconds. It was because of the early degradation of PFRS to produce phosphate which could promote a heat-protective char layer on the surface of PLA. Seen from Fig. 5 and 6, PHRR of neat PLA appeared at 419 kW m−2 and THR was 70.3 MJ m−2. When 15 wt% PFRS was added, the PHRR of PLA reduced to 316.6 kW m−2 and THR decreased to 61.5 MJ m−2. And then different proportions of APP and PFRS were added into the system, it is found that PLA systems have achieved further declines of PHRR and THR. The PHRR of PLA/3.8PFRS/11.2APP has decreased by 46% and 40% compared with that of neat PLA, respectively. In addition, the mass loss curves of PLA and PLA blends are displayed in Fig. 7. The combination of PFRS and APP could increase the residue weight of PLA with varying degrees. Among PLA/PFRS/APP samples, PLA/3.8PFRS/11.2APP presented the maximum final residue of 22.6 wt% while that of PLA/15PFRS and PLA/15APP was 6.2 wt% and 19.4 wt%, respectively. The improvement of the residue weight may be the important factor for its excellent flame-retardant properties.
In addition, the Fire Growth Rate (FIGRA) index was proposed to estimate the fire hazard of PLA blends more clearly. FIGRA was calculated by the ratio of PHRR and the time at peak heat release occurs, which became a heat acceleration parameter to judge both the scale of a fire and the predicted fire spread rate in reality. The higher the FIGRA value is, the quicker the fire spreads and propagates.38–40 PLA/3.8PFRS/11.2APP sample had a minimum FIGRA value of 1.4 kW m−2 s−1, which was lower than that of PLA/15PFRS and PLA/15APP. It indicated that PLA/3.8PFRS/11.2APP had a relative slower speed of fire propagation.
All above change trends were similar to the results of LOI and vertical burning test. So it was concluded that there existed a most appropriate PFRS/APP weight ratio (3.8/11.2) of intumescent flame retardant PLA systems, which had the best fire-resistant properties with the suitable proportion of acid source, carbon source and gas source. When adding 15 wt% PFRS or APP into PLA matrix alone, the flame retardancy of the system was unsatisfactory due to the absence of gas source or carbon source.
![]() | ||
Fig. 8 Digital photos of the residues after cone test for (a) PLA, (b) PLA/15PFRS, (c) PLA/15APP, (d) PLA/7.5PFRS/7.5APP and (e and f) PLA/3.8PFRS/11.2APP. |
Raman spectroscopy is a significant approach to characterize carbonaceous materials. The structure of char residue was presented by Raman spectra in Fig. 9. We can see two remarkable peaks at 1350 and 1580 cm−1, regarding as D and G peaks. The ratio of the relevant intensity of D to G peak (ID/IG) was used for assessing the graphitization degree of char residue. A lower ratio of ID/IG indicates the higher graphitization degree and thermal stability of char structure.42 For PPA/15PFRS, the ID/IG value was about 0.91. The incorporation of APP had a noteworthy impact on the intensity ratio ID/IG such as the ID/IG values of PLA/7.5PFRS/7.5APP and PLA/3.8PFRS/11.2APP reduced from 0.91 to 0.76 and 0.71, respectively, which were higher than that of PLA/15APP (0.85). This further implied that a higher graphitized carbons in the char layer of PLA/3.8PFRS/11.2APP composite, which was able to hinder the transfer of volatile and heat flux during the PLA combustion.
![]() | ||
Fig. 9 Raman spectra of the char residues of (a) PLA/15PFRS, (b) PLA/7.5PFRS/7.5APP, (c) PLA/3.8PFRS/11.2APP and (d) PLA/15APP. |
Scanning Electron Microscopy (SEM) was further applied to investigate the morphologies of the char residues after cone calorimeter tests, as shown in Fig. 10. Obviously, PLA/15PFRS had a poor char layer with many large holes and cracks. However, a distinct improvement on the quality of char layer for PLA/PFRS/APP composites was achieved. It could be seen that the holes and cracks became remarkably shrunken on the surface of the char residue of PLA/3.8PFRS/11.2APP composite and the char layer became more smooth and coherent. Moreover, many folds could be found in the char structure of PLA/3.8PFRS/11.2APP, which might be the intumescent bubbles broke during the burning because of the inner pressure of char residue. These coherent and intumescent features together rendered the charred residue with excellent barrier against the transmission of heat and volatiles, which was in agreement with the results of Raman spectra.
![]() | ||
Fig. 10 SEM micrographs of the residues after cone calorimeter test for PLA/15PFRS (a and c) and PLA/3.8PFRS/11.2APP (b and d). |
The above analysis of flammability and char residue revealed that the combination of 3.8 wt% PFRS and 11.2 wt% APP constituted an effective IFR system and hence facilitated the formation of a compact char layer. This compact char layer was helpful for condensed phase mechanism to play its role.
Sample | Tonset (°C) | Tmax (°C) | Residue weight at 600 °C (wt%) | The maximum weight loss rate (%/min) | |
---|---|---|---|---|---|
Experimental | Theoretical | ||||
PLA | 334.3 | 369.4 | 1.6 | 0 | 60.0 |
PLA/15PFRS | 315.7 | 368.7 | 6.1 | 7.4 | 54.7 |
PLA/3.8PFRS/11.2APP | 329.3 | 368.4 | 9.9 | 5.4 | 52.9 |
In order to clarify the gas-phase actions of PFRS and PFRS/APP systems, TG-FTIR was employed to study the evolved gas products of PLA and its composites during thermal degradation in N2. Fig. 12(a) presented the FTIR spectra of gas products at Tmax. It was obvious that the main degradation products for flame-retardant PLA were not altered compared with those of pure PLA. However, there was a significant delay and decrease of the peak appeared at 3002 cm−1 (C–H stretching) for flame-retardant PLA, as shown in Fig. 12(b). Pure PLA decomposed to release many hydrocarbons into gas phase from 15 min to 19 min, while the absorbance of hydrocarbons for flame-retardant PLA had a distinct decrease and delayed until 16 min. It implied that flame retardants could slow down the PLA degradation, and more hydrocarbons left in solid phase to form charring residues. Fig. 13 and 14 exhibited the TG-FTIR spectra of flame-retardant PLA during the timeframe of thermal degradation. Clearly, PLA/15PFRS could generate the PO (1258 cm−1) volatiles from 17 min to 19 min, which were deemed as free radical scavengers and had excellent quenching effect for flame-inhibition in gas phase.43,44 However, there were no peaks at 1258 cm−1 of PLA/3.8PFRS/11.2APP during the degradation process, indicating the presence of phosphorus-containing fragments were left in solid phase to catalyze the char production of PLA as discussed in thermal gravimetric analyses. Furthermore, this char residue prevented hydrocarbons entering into gas phase and hence there was a sharp drop of the absorbance in Fig. 12(b). All above came to a conclusion that the flame retardant mechanism of PFRS was depending on the simultaneous actions in gas phase and condensed phase, while PFRS/APP system was mainly related to condensed-phase mechanism.
![]() | ||
Fig. 12 (a) FTIR spectra of gas products at Tmax and (b) absorbance of hydrocarbons for PLA and its composites. |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c7ra12582h |
This journal is © The Royal Society of Chemistry 2018 |