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Pyrolysis products and thermal degradation mechanism of intrinsically flame-retardant carrageenan fiber

Zhixin Xue*ab, Weiwei Zhangab, Miao Yanab, Jingjing Liuab, Bingbing Wangbc and Yanzhi Xia*b
aCollege of Chemistry and Chemical Engineering, Qingdao University, Qingdao 266071, China
bResearch Institute of Marine Fiber Novel Materials, Qingdao University, Qingdao 266071, China. E-mail: xyz@qdu.edu.cn
cYantai Tayho Advanced Materials Group Co., Ltd, No. 9 Heilongjiang Rd., Yantai EDTA 264000, China

Received 24th January 2017 , Accepted 5th May 2017

First published on 10th May 2017


Abstract

Carrageenan fiber (CAF) was prepared by a wet spinning method to develop an excellent flame-retardant material. In order to investigate the flame-retardant mechanism of CAF, a series of tests were carried out. The values of limiting oxygen index (LOI), total heat release (THR), and total smoke release (TSR) of CAF reached up to 52, 2.9 MJ m−2, and 2.5 m2 m−2, respectively, while there was no Time To Ignition (TTI) in cone calorimeter (CONE). These results indicate that CAF exhibits superior flame-retardant performance than other alginate fibers. Thermogravimetry, differential scanning calorimetry, Fourier transform infrared spectroscopy (TG-DSC-FTIR) and pyrolysis-gas chromatography-mass spectrometry (Py-GC-MS) tests were performed in order to explore the pyrolysis mechanism. The results show that CAF absorbed more heat and produced more carbon residue than calcium alginate fiber (ALF) and agar fiber (AGF) in the process of thermal degradation. In addition, in the current work, we have explored the possible flame-retardant mechanisms which can be attributed to sulfonyl free radical (SFR), carbon residue, barium sulfate, water vapor, and carbon dioxide.


1. Introduction

The increasing demand for novel functional materials and environmental protection materials has constantly encouraged people to engage in the research for new products. A few studies reported in the literature have found that carrageenan fiber (CAF) is a renewable and non-polluting natural seaweed product in contrast with the conventional petroleum-based fibrous materials.1 Hence, CAF shows an extensive potential to be applied in textile fabrics, such as fire-protection suits, bedclothes, curtains and carpets.

Carrageenans belong to the biopolymer family and have been widely used as food additives for their beneficial health properties. The flame retardancy is another innovative feature of carrageenans, which is well worth studying in order to produce flame-resistant materials. Carrageenan is a sulphated polysaccharide and has a random coil conformation in aqueous solutions when the temperature of the solution is higher than the gelation temperature.2,3 Carrageenans are extracted from red algae, and the most important members are kappa (κ), iota (ι), and lambda (λ).4–6 Additionally, they carry a different number of sulfate groups. The structures of the macromolecules are composed of linear polysaccharides of alternating 3-linked β-D-galactopyranosyl residues and 4-linked α-D-galactopyranosyl or 3,6-anhydro-galactopyranosyl residues, while the sulfate esters are introduced in different positions.7,8 Due to the polyanionic characteristic of sulfate bases, carrageenans exhibit many biological activities, such as acting as an anti-coagulant or anti-viral.9–14 Also, sulfate bases can play a key role in flame retardancy when carrageenans are spun into threads.15,16

Recently, most of textiles have been dealt with phosphorus-based flame retardant, halogen-based flame retardant, inorganic flame retardant, and nitrogen-containing flame retardant to reduce the flammability.17–24 The applications of those flame retardants have been the most efficient ways of reducing the economic loss and ensuring personal security when the fire accident happened suddenly. However, once burned, some of the flame retardants produce corrosivity, carcinogen, and poisonous gas,18 which violate the principle of environmental protection. Nevertheless, CAF possesses the function of flame retardancy and pro-environment, which will be attached importance to its practical application. This double-win behavior has attracted much attention in recent time and continues to attract significant interest in the field of flame retarded applications, especially fire resistant fiber.

In recent years, Professor Xia and coworkers have explored the flame-retardant mechanism of alginate fibers and cellulose fibers.25–27 The group has already shown that divalent metal ions play an important role in the flame retardancy and thermal stability of alginate fibers. Calcium alginate fiber (ALF), barium alginate fiber and zinc alginate fiber have good fire-retardant properties without addition of other conventional flame retardants.28–30 The aforementioned results proved that the addition of divalent metal ions effectively improved the flame-retardant properties of the fabrics. Coincidently, coagulation bath, in the presence of barium ions, was applied to wet spinning to obtain the CAF with divalent metal ions (barium ions) into its molecular structure.

In the current study, CAF produced through wet spinning method, is demonstrated as a novel and an extremely efficient flame retardant material.31 The discussed method proved to be exceptionally advantageous when we reasonably utilize the viscoelasticity and gelation of carrageenan solution.32–37 In regards to the flame-retardant properties of the material, molecules with higher content of sulfate ester can deliver more active flame retardant atoms. Agar is another polysaccharide extracted from red algae, whose molecular structure is similar to the carrageenan, except lower sulfate content.

In this study, the flame-retardant properties of agar fiber (AGF) and ALF were investigated for the purpose of comparisons with CAF. Meanwhile, the flame-retardant mechanism of CAF and its pyrolysis mechanism are also investigated in the current work.

2. Experimental section

2.1 Materials

Kappa carrageenans (κ-) were purchased from Shishi Universal Joan Glue Industrial Co., Ltd (Quanzhou, China). Agar (biological reagent) was obtained from Lanji Technology Development Co., Ltd (Shanghai, China). Barium chloride, dimethyl sulfoxide, ethanol, and sodium hydroxide were purchased from Sinopharm Chemical Reagent Co., Ltd (Shanghai, China), and these reagents were all analytical grade. Calcium alginate fiber (ALF) was supplied by Kangtong Marine Fiber Co., Ltd.

2.2 Preparation of spinning dope

The solutions including κ-carrageenan (9 wt%, 800 mL) and agar (12 wt%, 800 mL) were prepared as follows. Measured amount of κ-carrageenan powder (72 g) was dispersed in sodium hydroxide solution (2 mol L−1) by stirring at 50 °C for duration of 2 h to obtain homogeneous carrageenan dope. For the preparation of agar solution, 96 g agar powder was dissolved into dimethyl sulfoxide (704 mL) at 95 °C for 2 h using a magnetic stirrer. Thereafter, the equable solutions were degassed in a vacuum oven under reduced pressure for about 30 min. Finally, the dopes were hermetically laid aside for 12 h to be applied to spinning.

2.3 Fabrication and post-processing of spinning fibers

The fibers were produced by coagulation method using custom-made wet spinning equipment in Fig. 1, and process diagram was shown in Fig. 2(a).
image file: c7ra01076a-f1.tif
Fig. 1 Custom-made wet spinning equipment.

image file: c7ra01076a-f2.tif
Fig. 2 (a) The scale-up process of CAF from solution to fiber. (b) The sample preparation processes of LOI and CONE.

The spinning dopes were extruded through a commercial spinneret with thirty orifices, and the nitrogen pressure of 0.5 MPa was controlled by a pressure regulator in order to squeeze out the dope evenly. Barium chloride was used as a precipitator, and it was dissolved in coagulating bath (7 wt%) and stretch bath (4 wt%). The revolving speeds of metering pump, the first roller, and the second roller were set at 4.97 rpm, 10 rpm, and 12 rpm, respectively. In the next step, spinning operation could be implemented in accordance with the literature.31 Thereafter, the as-spun fibers were orderly washed by alcohol (50%, v/v) and alcohol (95%, v/v) to remove residual metal ions. Finally, the obtained fibers were dried at 60 °C to a constant weight.

2.4 Characterization

Limiting oxygen index (LOI) was recorded using HC-2 type instrument according to international standard ASTM D2863. The fiber sample (3 g) was cut into strip (10 × 3 × 0.4 cm) and placed in a combustor (Fig. 2(b)), where a mixture of oxygen and nitrogen flows in an upward direction. The volume content of the oxygen was adjusted to keep the lowest oxygen concentration that just supports sustained burning.

The cone calorimeter (ISO 5660 standard) was used to evaluate the combustion behavior of fabric. Specimens with dimensions of 10 × 10 × 0.4 cm were used in all tests. According to the ISO 5660 standard, normally applied for the study of combustion behavior in plastic specimens using the cone calorimeter, the fibers (10 g) were cut to a dimension size of 10 × 10 cm and placed over the middle of an aluminum foil of 10.2 × 10.2 cm with the shiny side toward the specimen. Then the specimen was pressed into a sheet with thickness of 0.4 cm (Fig. 2(b)). The specimens were burned for all the experiments with horizontal orientation in air atmosphere at predetermined heat fluxes of 35 kW m−2.38

Scanning Electron Microscope (SEM, Hitachi TM-3000, Japan) were used to record the morphology of fibers at a beam voltage of 15 kV after gold sputtering. X-ray diffraction (XRD, DX2700, China) with an accelerating voltage of 40 kV and a current of 30 mA under Cu-Xα radiation was used to scan crystalline structure. The control parameters (angle (2θ): 10–80; stepping angle: 0.01; sampling time: 0.3) were set appropriately.

The TG-DSC-FTIR (STA6000-Frontier, PE) measurements were conducted to record the thermal variation and functional information about the products which appeared in the process of temperature programming. About 5 mg of the samples, under the atmosphere of nitrogen, were heated from room temperature to 900 °C at a heating rate of 20 °C min−1. The fast pyrolysis analyzer (Py, Frontier Lab EGA/PY-3030D, Japan) was coupled with GC-MS (QP2010Ultra, Shimadzu Corporation) systems to investigate the distribution of volatiles. The pyrolysis parameters were as follows: pyrolysis time: 0.5 min. The GC-MS parameters were as follows: GC column (ZB-5HT): 30 m × 0.25 mm × 0.25 μm; GC temperature program: initial temperature starting at 35 °C (kept for 3 min); the heating rate: 10 °C min−1; carrier gas: high-purity He with the flow rate of 1.0 mL min−1; the scanning mode of ion source: full scan (29–600 m/z). Thereafter, the compounds were determined via characterization GC-MS spectrums according to the database of NIST library.

3. Results and discussion

3.1 Flame-retardant data and the influential factors

The combustion data of ALF was acquired via LOI and CONE tests. According to previous reports, ALF possesses good flame-retardant properties.30 But, we observe that CAF presents the maximum value (52) for LOI when compared with ALF (46) and AGF (18.5). The values of LOI and CONE revealed significant differences in the fibers as shown in Table 1.
Table 1 The data of limiting oxygen index, cone calorimeter, and element content of different samples
Parameters Samples
AGF ALF CAF
a The minimum concentration of oxygen in an oxygen/nitrogen gas stream mixture to keep combustion.b The time needed to achieve sustained flame combustion at a particular irradiance.c The sample keeping red state without flame.d The total heat release in 0–225 s.e The elements were tested after CONE.
LOIa 18.5 46 52
TTIb (s) 4 108 Red statec
Peak HRR (kW m−2) 265 32 22
THR225 sd (MJ m−2) 20 9.6 2.9
TSR225 s (m2 m−2) 0.8 12.1 2.5
Mean MLR (g s−1) 0.1 0.05 0.03
Sulfur content (%) 0.27 0 6.2
Ba/Ca contente (%) 19.4 (Ba) 36.2 (Ca) 23.3 (Ba)


There was no TTI for CAF, keeping red state for the complete duration of test process in contrast with ALF (108 s) and AGF (4 s). The results suggested a surprising performance of CAF in regards to difficulty of combustion. In addition, the results of peak HRR, THR225 s, TSR225 s, and Mean MLR were determined to be 22 kW m−2, 2.9 MJ m−2, 2.5 m2 m−2, and 0.03 g s−1, respectively for CAF (Table 1 and Fig. 3). The results indicated CAF had low heat release, smoke release, and mass loss in the process of combustion.


image file: c7ra01076a-f3.tif
Fig. 3 The cone calorimeter data of CAF/ALF/AGF. (A) Heat release rates (HRR); (B) total heat release (THR); (C) total smoke release (TSR); (D) mass loss rate (MLR).

In view of the AGF, owing to the flammable characteristic and high heat release quantity, it burned more completely. And the mass was primarily lost in the form of carbon dioxide (gas state), instead of smoke due to low TSR as shown in Fig. 3(C). Therefore, AGF showed higher mean MLR (0.1 g s−1) and lower TSR225 s (0.8 m2 m−2) than the other two fibers (as shown in Fig. 3(D) and (C)).

The HRR and THR trend curves of CAF shown in Fig. 3(A) and (B) are lower than that of ALF and AGF. In addition, CAF showed strong smoke suppression property in comparison with ALF (Fig. 3(C)). The phenomena indicated that there is enough time to escape in the case of sudden fires, and the flame resistance can reduce the property damage. In conclusion, the flame retardancy of CAF is superior to that of ALF and AGF.

In further investigations, we observed that pronounced changes have taken place in fiber morphology after combustion. As shown in Fig. 4(A1)–(B3), the shapes of the fibers were destroyed to some degree after combustion. Fig. 4(B1) shows that AGF completely lost its morphology (presenting fragmented feature). However, the residues of ALF and CAF shown in Fig. 4(B2) and (B3) present relatively well morphologies which are coated with dense layer. The layer consisted of amorphous round particles or lamellar particles which closely arrange on the surface of fiber residue. Nonetheless, the surfaces of initial fibers (Fig. 4(A2) and (A3)) were relatively smooth. The dense layer acted as a barrier to prevent the heat and oxygen into the fiber making the fiber produce more carbon residue. Therefore, the inside fibers turned more into black carbon residue in contrast with the surface fibers (seen from the insets of Fig. 4(B2) and (B3)).


image file: c7ra01076a-f4.tif
Fig. 4 SEM and optical (insets) morphology of fibers before (A1/A2/A3) and after burning (B1/B2/B3). (A1)/(B1) Agar fiber (AGF); (A2)/(B2) calcium alginate fiber (ALF); (A3)/(B3) carrageenan fiber (CAF). The XRD (C1/C2/C3) of fiber residues. (C1) AGF residue; (C2) ALF residue; (C3) CAF residue.

In order to further investigate the particle composition of surface residue, X-ray diffraction was conducted under reasonable test parameters. All identified peaks in each curve could be indexed to BaSO4 (Fig. 4(C1)), CaCO3 (Fig. 4(C2)), and BaSO4 (Fig. 4(C3)), respectively. The surfaces of fiber residue are covered with CaCO3 (ALF) and BaSO4 (CAF), which are proved again in Fig. 5. For AGF, the content of sulfur elements which exists in raw material was very little (Table 1). The residue of AGF was almost no dense layer, which was one of the reasons for its poor flame retardancy. On the contrary, the dense layer of CAF was probably the aggregation of particles of BaSO4, which could work together with carbon residues to take part in fire retardation.28,29 Fig. 5(b1)–(b4) show that the surfaces of CAF combustion residue are covered with BaSO4 and a small amount of carbon residue. The most of carbon residues still remain in the interior of burned CAF. In addition, carrageenan molecules have certain number of sulfate ester, which could be another plausible reason behind better flame retardancy of CAF as compared to ALF or AGF.15,16


image file: c7ra01076a-f5.tif
Fig. 5 SEM-EDS test of the surfaces of ALF (A) and CAF (B) combustion residue.

3.2 TG-DSC-FTIR analysis

In response to the discovery of unexpected results, the flame-retardant mechanism of CAF was explored with the purpose of deeper understanding of flame resistance. The results of thermal analysis data demonstrated significant differences between three kinds of fibers (Fig. 6). Fig. 6(A)–(C) indicate that all the samples exhibited initial weight loss and showed an endothermic peak on the DSC curve at about 100 °C, which can be attributed to the volatilization of absorbed water of fibers. In the next step, the weight loss of AGF was up to 55% between 200 and 400 °C which might be associated with the fracture of glycosidic bond and hexatomic ring, dehydration, and decarbonylation.28,39 Meanwhile, a great amount of heat was released and a broad exothermic peak with hysteresis appeared after 400 °C, which was not conducive to the flame retardancy of AGF. As shown in Fig. 6(B), similar to CAF (Fig. 6(C)), there were four stages of mass loss in the process of temperature-rise, which can be seen from the curve of DTG. The maximum weight loss rates of AGF, ALF and CAF, located in the second stage of the DTG curves, were about 12% per min, 11.5% per min and 30% per min, respectively, while the corresponding weight losses seen from the curves of TG were about 55%, 35% and 13%, respectively. These phenomena can be attributed to the better thermostability of CAF. Fig. 6(C) shows that CAF exhibited a large endothermic peak in the fourth stage when the temperature rose to 800 °C, and the weight loss was about 12% in this stage which can be attributed to the further decomposition of carbon residue. These results suggested that CAF exhibited superior high-temperature resistance due to the endothermic effect under high temperature. Also, as observed from the curves of TG, when the temperature was up to 700 °C, the rest mass of the three kinds of fiber was 25% (AGF), 35% (ALF), and 45% (CAF), respectively. These results indicated that many carbonized products were formed for CAF, suggesting another plausible reason behind flame-retardant performance.
image file: c7ra01076a-f6.tif
Fig. 6 TG-DSC thermograms of AGF (A), ALF (B), and CAF (C) and three-dimensional diagram of TG-FTIR of AGF (a), ALF (b) and CAF (c).

FTIR technique was utilized for characterization of gaseous pyrolysis products of polymers, which exhibits different infrared characteristic peaks at different positions. Overall pyrolysis products can be easily found from the three-dimensional diagram of TG-FTIR. As observed in Fig. 6(a) and (b), AGF and ALF produced large amounts of pyrolysis products at the beginning time. In contrast, CAF began to produce a significant amount of pyrolysis gas at around 2000 s (Fig. 6(c)), and there were distinct absorption peaks at 2340 cm−1, 2200 cm−1, 1700 cm−1 and 1100 cm−1. Additionally, the pyrolysis products of CAF were less than that of AGF, as shown in Fig. 6(a) and (c). The results also showed that CAF had better high temperature resistance than AGF or ALF.

In the above context, infrared spectra of special groups which were recorded near the temperatures of major weight loss rate were compared in Fig. 7. For example, AGF: 100, 200, 300, and 500 °C were typical temperature according to Fig. 6(A), and the temperature of the maximum weight loss rate was 300 °C; ALF: 100, 250, 550, and 750 °C were typical temperature according to Fig. 6(B), and the temperature of the maximum weight loss rate was 250 °C; CAF: 100, 210, 280, 725, and 780 °C were typical temperature according to Fig. 6(C), and the temperatures of the maximum weight loss rate was 210 and 780 °C.


image file: c7ra01076a-f7.tif
Fig. 7 FTIR spectra of thermal degradation products of fibers in different temperatures (programmed temperature in accordance with TG in Fig. 6). (a) AGF; (b) ALF; (c) CAF; (d) CAF residue.

As shown in Fig. 7, the maximum absorption intensity of three kinds of fiber was recorded around 300 °C (AGF), 250 °C (ALF), and 725 °C (CAF), respectively. The broad band at 3500–3800 cm−1 was related to O–H stretching vibration of pyrolysis gas; the peak at 2340 cm−1 was attributed to CO2, and the peak around 1700 cm−1 was assigned to C[double bond, length as m-dash]O stretching vibration which was rather stronger in Fig. 7(a) (300 °C). The peak at 2200 cm−1 was determined to C[triple bond, length as m-dash]C stretching vibration or gaseous phase CO which was relatively stronger in Fig. 7(c) (725 °C). The bands at 1000–1300 and 1620–1680 cm−1 which was overlapped with the absorbance peak of C[double bond, length as m-dash]O were identified as C–O and C[double bond, length as m-dash]C, respectively, and they were distinct in Fig. 7(a). Based on the results in Fig. 7(a)–(c), we can conclude that with the rise in temperature, the concentration of pyrolysis gas first increases and then decreases with further rise in temperature. Also, AGF generated many complex and abundant pyrolysis products at 300 °C which was in accordance with Fig. 6(a). CAF released less pyrolysis gas at relatively low temperature range, and significant amount of pyrolysis gas was produced in the high temperature range (Fig. 6(c) and 7(c)). The results further demonstrated that CAF had better flame retardancy than the other two fibers. Moreover, high concentration of carbon dioxide in pyrolysis gas further promoted the flame-retardant ability for CAF.

FTIR spectra of fiber residues are presented in Fig. 7(d). Since CAF produces bulk of carbon residues which can form conjugate systems, the system promoted the band at 1620–1680 cm−1 to move around 1600 cm−1 and the conjugate system further improved the stability of carbon residues.40–43 Moreover, it was noted that there was distinct absorption band at 1040–1200 cm−1 which was attributed to S[double bond, length as m-dash]O stretching vibration. This group can exert an important influence on pyrolysis mechanism of carrageenan.15,16 Also, S[double bond, length as m-dash]O intensity became stronger with an increase in temperature. The groups of S[double bond, length as m-dash]O primarily remain in residue rather than releasing in pyrolysis gas, which fully embodies the principle of environmental protection.

3.3 Py-GC-MS analysis

In order to investigate the primary components of gaseous products in the pyrolysis process of CAF, pyrolysis gas chromatography and mass spectrometry (Py-GC-MS) analysis were conducted at 250 °C and 750 °C (near the higher value of weightlessness) which were selected according to the curve of TG. AGF and ALF which exhibited relatively poor flame retardancy in comparison with CAF were not analyzed in Py-GC-MS test. In comparison with mass spectra fragmentation pattern with NIST library and published data, the highest similarity of compound identification was obtained. The gas chromatogram demonstrating the peaks of different retention time is displayed in Fig. 8, and the major characteristic compounds are summarized in Table 2.
image file: c7ra01076a-f8.tif
Fig. 8 Py-GC-MS spectra of CAF under the different pyrolysis temperatures. (a) 250 °C; (b) 750 °C (the pyrolysis products of 6–12 are not listed in MS spectra).
Table 2 Py-GC-MS main analysis results of CAF at 250 and 750 °C
Fragment structure Name T = 250 °C T = 750a °C
Time (min) Area (%) Time (min) Area (%)
a The pyrolysis product of CO2 was not computed in order to highlight the other compounds at 750 °C.
image file: c7ra01076a-u1.tif (1) Carbon dioxide 1.48 72.06
image file: c7ra01076a-u2.tif (2) Butan-2-ol 23.68 2.96
image file: c7ra01076a-u3.tif (3) Cyclohexade-1,9-diene 24.00 10.35
image file: c7ra01076a-u4.tif (4) 4-Butyl-cyclohexene 24.28 11.23
image file: c7ra01076a-u5.tif (5) 4-Isobutyl-cyclohexene 27.70 3.39
image file: c7ra01076a-u6.tif (1) 2-Oxo-3-sulfo-propionic acid 1.47 23.92
image file: c7ra01076a-u7.tif (2) Pent-3-yn-1-ol 1.56 15.90
image file: c7ra01076a-u8.tif (3) Acetic acid 3-methyl-but-3-enyl ester 1.76 12.35
image file: c7ra01076a-u9.tif (4) Cyclopenta-1,3-diene 1.92 9.12
image file: c7ra01076a-u10.tif (5) 2-Methyl-furan 2.34 17.31
image file: c7ra01076a-u11.tif (6) Hexa-1,3-dien-5-yne 3.14 2.94
image file: c7ra01076a-u12.tif (7) 2,5-Dimethyl-furan 3.93 3.66
image file: c7ra01076a-u13.tif (8) Pentan-2-one 4.08 1.44
image file: c7ra01076a-u14.tif (9) 2,4-Dimethyl-furan 4.18 1.85
image file: c7ra01076a-u15.tif (10) Spiro[2.4]hepta-4,6-diene 5.12 3.33
image file: c7ra01076a-u16.tif (11) 1-Furan-2-yl-ethanone 6.15 1.31
image file: c7ra01076a-u17.tif (12) 3-Methylene-1-vinyl-cyclopentene 7.33 0.92


Fig. 8(a) shows that when the pyrolysis temperature was 250 °C, there were fewer peaks in the gas chromatogram as compared to 750 °C (more than 20 peaks). These results indicated that CAF still had good stability at 250 °C. As shown in Table 2, when the temperature was set at 250 °C, the primary component of pyrolysis gas was CO2 (about 72.06%) which played an important role in preventing combustion. The primary pyrolytic products (shown in Fig. 8 and Table 2) were as follows: (a): (1) carbon dioxide, (2) butan-2-ol, (3) cyclohexadeca-1,9-diene, (4) 4-butyl-cyclohexene, (5) 4-isobutyl-cyclohexene; (b): (1) 2-oxo-3-sulfo-propionic acid, (2) pent-3-yn-1-ol, (3) acetic acid 3-methyl-but-3-enyl ester, (4) cyclopenta-1,3-diene, (5) 2-methyl-furan, (6) hexa-1,3-dien-5-yne, (7) 2,5-dimethyl-furan, (8) pentan-2-one, (9) 2,4-dimethyl-furan, (10) spiro[2.4]hepta-4,6-diene, (11) 1-furan-2-yl-ethanone, (12) 3-methylene-1-vinyl-cyclopentene. These compounds could be primarily divided into furan, ketone, unsaturated hydrocarbon, hydroxyl compound, acids, and they contain the functional information of C[double bond, length as m-dash]C, C[double bond, length as m-dash]O, C[triple bond, length as m-dash]C and S[double bond, length as m-dash]O which were in accordance with the data of TG-FTIR in Fig. 6(c) and 7(c). The mass of these compounds was smaller than that of carbon residue which was incumbent on the surface of the fiber to stop the unceasing production of pyrolysis gas. As shown in Table 2, at 750 °C, 2-oxo-3-sulfo-propionic acid was the primary products along with carbon dioxide whose total yield was 23.92%. The results indicate that sulfate group might have a great influence on flame-retardant mechanism because of easy formation of sulfonyl free radical (SFR) under heating conditions. SFR was produced under the heating conditions, and it was apt to combine with hydroxyl radical (HR) generating sulfo group (Scheme 1c). The reduction of HR was in favor of fire resistance. In the next step, sulfo group combined with carbon monoxide and hydrogen free radical (HFR) reproducing SFR along with the production of CO2 and H2O.44–49 The pyrolysis mechanism is presented in Scheme 1(a)–(d). Moreover, sulfate groups can combine with barium ions generating a layer of barium sulfate (seen from Fig. 4(B3) and (C3) and 5(B)), which can prevent the exchange of matter and energy and stop them in and out of the fiber.


image file: c7ra01076a-s1.tif
Scheme 1 Schematic representation of proposed pyrolysis mechanisms of CAF. (a) Polymeric macromolecule of CAF. (b) The main cracking paths under the condition of heating. (c) Pyrolysis mechanisms and pyrolysis products. (d) The explanation of some cracking intermediates.

In accordance with the TG-DSC-FTIR and Py-GC-MS analyses in inert gas atmosphere, pyrolysis mechanisms of CAF are summarized in Scheme 1. It shows the mechanism of carbon residue (condensed phase mechanism), SFR (the gas phase mechanism), barium sulfate (condensed phase mechanism), water vapor (the gas phase mechanism), and carbon dioxide (the gas phase mechanism) which are marked by multigonal star pattern in Scheme 1, and three primary cracking paths are listed in Scheme 1(b). The intermediate products were further degraded under the condition of heating through bond breaking, ring opening, dehydration, desulfuration, ring formation and so on. Then, some of the molecules and fracture fragments, seen from Scheme 1(c), were produced and detected. They have great guiding significance for flame-retardant mechanism of CAF in the air atmosphere.

4. Conclusion

The data of LOI (52) and CONE showed that CAF exerts difficult-flammability and low heat yield in contrast with AGF or ALF. The results of TG showed that when the temperature was up to 700 °C, the rest masses of the three kinds of fiber were 25% (AGF), 35% (ALF), and 45% (CAF), respectively. In comparison with the previous reports on flame-retardant alginate fiber, CAF demonstrated much stronger flame retardancy, most likely due to the distinct flame-retardant mechanisms such as SFR, carbon residue, barium sulfate, and carbon dioxide. SFR can reduce the concentration of HFR to terminate the combustion. Moreover, unburned fiber was wrapped by carbon residue and barium sulfate which were capable of preventing heat going into the fiber. In general, CAF, a new type of flame-retardant material, is showing a great utilization potential. Next, we will try to add other metal ions and flame retardants to further improve the flame retardancy of CAF. In particular, the flame-retardant mechanism of CAF should be further explored.

Acknowledgements

This work is supported by the National Natural Science Foundation of China (50803030), the Postdoctoral Science Special Foundation of China (201104581), the Postdoctoral Science Foundation of China (20100471495), the Program for Taishan Scholar of Shandong Province of China, and the Program for Changjiang Scholars and Innovative Research Team in University of China (No. IRT0970). The authors are also thankful to the International Cooperation Program for Excellent Lectures of 2012 by Shandong Provincial Education Department of China and the Special Fund for Self-directed Innovation of Shandong Province of China (No. 2013CXB80201).

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