Abstract
This study proposes a novel strategy for the value-added utilization of converter OG sludge by incorporating it as a flame-retardant additive in rigid polyurethane foam (RPUF). A series of RPUF/OG composites were fabricated via a one-step all-water foaming technique. The effects of OG sludge on the thermal stability, combustion behavior, and flame retardant properties of RPUF were systematically investigated using multiple analytical methods, including limiting oxygen index (LOI) test, vertical burning test (UL-94), thermogravimetric analysis (TG), and cone calorimeter test (CCT). The results show that OG sludge can significantly enhance the fire safety of the composites. While traditional metrics like the limiting oxygen index showed limited improvement, CCT results indicate that the peak heat release rate (pHRR), total heat release (THR), and total smoke production (TSP) of the RPUF/OG50 composite decrease significantly by 16.5%, 24.1%, and 43.6%, respectively. This confirms the effectiveness of OG sludge in suppressing fire intensity and smoke generation. TG reveals that OG sludge improves the thermal stability of RPUF composites, with a residual char yield of up to 21.7 wt% at 800°C. Scanning electron microscopy (SEM) and Raman spectroscopy analyses demonstrate that the complex metal oxides in OG sludge enhance the compactness of the char residue of RPUF composites, forming a stable barrier layer that inhibits the transport of heat and substances during the combustion of the composites. This study provides a new approach for the high-value and sustainable utilization of OG sludge, and offers directions for the development of flame-retardant RPUF composites for building thermal insulation applications.
Introduction
The iron and steel sector produces a diverse range of solid wastes. Currently, most of the dust and sludge is disposed of simply by landfilling. Not only does this way consume a huge quantity of land resources, but it also constitutes a substantial threat to human health and the natural environment. 1 At present, the reuse and utilization of converter OG sludge in China mainly make use of a number of technologies. They are reverse sintering; processing zinc - containing dust and sludge with the help of rotary hearth furnaces, rotary kilns, and cold briquetting technology; and the digestion approach of adding lime powder to converter OG sludge.2–4 Most of these technologies require in depth treatment of OG sludge, and their added value needs to be enhanced. Therefore, promoting the high value utilization of dust and sludge through green and low - carbon methods has become an urgent task, and it is also a key issue that the current metallurgical industry urgently needs to address. 5
Converter OG sludge is mainly composed of oxides formed by the oxidation of elements such as Fe, Ca, Si, and P in metallurgical raw materials, impurities introduced during the steel making process, and furnace lining materials that erode and fall off. Its main components are low valence iron oxide, calcium oxide, and a small amount of zinc oxide, phosphorus pentoxide, etc. 1 The metal oxide components discussed earlier have been extensively employed as flame retardant synergists within polymer composites. The origin of the flame retardant effect of metal oxides lies in their various functional characteristics, including physical shielding, 6 catalytic carbonization, 7 and chemical capture. 8 These mechanisms are essential for enhancing the flame retardant characteristics of materials, lowering smoke production, and reducing toxicity levels. 9 Therefore, being a blend of the aforementioned components, converter OG sludge holds extensive application potential in the realm of flame retardancy. 2
Notably, the utilization of various industrial solid wastes as fillers or flame retardant additives in polymers has gained significant attention.10,11 For instance, modified iron tailings have been used synergistically with ammonium polyphosphate (APP) to enhance the flame retardancy of thermoplastic polyurethane (TPU). 12 Similarly, sludge residue from wastewater treatment (digestate) has been incorporated into Poly (Lactic Acid) (PLA) as a synergistic additive with APP, improving fire performance. 13 In particular, fly ash (FA), another abundant industrial by-product, has been successfully incorporated into polymers like epoxy and polybutylene adipate terephthalate (PBAT) to improve flame retardancy, often showing synergistic effects with conventional flame retardants.12,14 These studies typically report the formation of stable protective char layers containing new crystalline phases, which enhance fire resistance. However, despite its complex metal oxide composition resembling a pre-designed synergistic system, the direct application of untreated converter OG sludge as a flame retardant filler in polymers, particularly in rigid polyurethane foam (RPUF), remains largely unexplored and represents a significant research gap. Therefore, exploring the feasibility and effectiveness of utilizing this unique, untreated OG sludge to address the flammability issue of RPUF is of great interest.
Rigid polyurethane foam (RPUF) is formed by the addition polymerization reaction of polyols and isocyanates.15,16 It has advantages such as good thermal insulation performance, low mass, good mechanical properties, and a simple preparation process. 17 It finds extensive application in various areas such as building exterior wall insulation, pipeline heat preservation, and the insulation of refrigerators, freezers, and water heaters.18,19 Nevertheless, RPUF shows weak fire resistant properties, with a relatively low limiting oxygen index (around 18 vol%). Additionally, it emits toxic gases like HCN and CO when burning. 20 These deficiencies have significantly hampered the widespread use of RPUF. 21 Consequently, enhancing the flame retardancy of RPUF and decreasing the emissions during its combustion are crucial problems that the industry urgently needs to solve.
Presently, the reactive type and the additive type serve as two commonly adopted strategies for enhancing the flame retardancy of RPUF. 22 Reactive flame retardants are made by chemically bonding flame retardant groups (hydroxyl, amino or epoxy groups, etc.) to the polyurethane molecular chain, so that the flame - retardant performance becomes an intrinsic property of the material. This can endow polyurethane foam with excellent flame - retardant properties during the foaming process.23–25 However, the preparation procedure of this approach is intricate and expensive, and the number of reactive flame retardants in the market is relatively small, with a limited range of choices. 19 Additive flame retardants usually refer to halogenated flame retardants, phosphorus flame retardants,26,27 metal hydroxides, 28 intumescent flame retardants, 29 expanded graphite (EG),30–32 organoclay 33 and other flame retardant substances are incorporated into polyurethane via the blending approach to enhance its flame retardant characteristics. Additive flame retardants do not engage directly in the foaming and curing reactions, instead, they provide a wider range of structural variations compared to reactive flame retardants. 34 In addition, their synthesis procedures are much simpler, and additive flame retardants have drawn significant interest within the industry due to their simplicity, dependability, and cost effectiveness.
In this work, we propose a novel and high-value strategy by employing untreated converter OG sludge directly as an additive flame retardant for RPUF. To the best of our knowledge, this is the first comprehensive study to systematically investigate the use of converter OG sludge in RPUF for enhancing flame retardancy. RPUF/OG sludge composites were prepared through a full water foaming technique. The limiting oxygen index (LOI), vertical combustion (UL-94), cone calorimetry (CCT), and scanning electron microscopy (SEM) were employed to investigate the flame retardant properties, combustion characteristics, and morphological changes of the RPUF/OG sludge composites. This study not only offers a novel approach for the high-value utilization of converter OG sludge but also demonstrates the fabrication of flame-retardant RPUF composites using metallurgical solid waste, contributing to both waste management and material science.
Experimental
Materials
Polyether polyol (LY-4110) and Triethylenediamine (A33) was obtained from Jiangsu Lvyuan New Material Technology Co., Ltd. Polymethylene polyphenyl isocyanate (PM-200) was obtained from Wanhua Chemical Group Co., Ltd. Silicone oil foam stabilizer (AK-8805) was obtained from Jining Hengtai Chemical Co., Ltd. Triethanolamine (TEOA) was obtained from Sinopharm Chemical Reagent Co., Ltd. Dibutyltin dilaurate (LC) was obtained from Air Products and Chemicals, Inc. The converter OG sludge was obtained from MaSteel (Group) Holding Co., Ltd. The as-received sludge was first dried in an oven at 105°C for 24 hours to remove moisture. Subsequently, it was manually ground using an agate mortar and pestle to break down agglomerates and obtain a fine powder suitable for blending with the polyurethane precursors. Distilled water was produced internally within the science lab.
Synthesis n of RPUF composites
Composition of raw materials of RPUF and RPUF/OG sludge composites (unit: g).
Characterization
Limiting Oxygen Index (LOI): The LOI of the composite materials was assessed with a JF-3 type oxygen index analyzer (produced by Nanjing Jiangning District Instrument Analysis Factory) in accordance with the ASTM D2863 standard. The specimens had dimensions of 10 × 10 × 127 mm3.
Vertical Combustion (UL-94): The vertical combustion behavior of the test samples was evaluated with a horizontal and vertical combustion tester (model CZF-3, made by Nanjing Jiangning District Instrument Analysis Factory) following the GB/T 2408 standard. The test specimens were characterized by dimensions of 127 × 13 × 10 mm3.
X-ray Diffraction (XRD): The mineral composition of the OG sludge was tested using a D8 ADVANCE X-ray single-crystal diffractometer (Bruker, Germany). The designated material employed was a Cu target, operating at a power level of 3 kW. The test angle scope spanned from 5° to 80°, and the precision of the 2θ angle was no more than 0.02°.
X - ray Fluorescence Spectroscopy (XRF): To study the chemical makeup of the converter OG sludge, an ARL Advant’X Intellipower TW3600 scanning X-ray fluorescence spectrometer (Thermo Fisher Scientific, USA) was put into use.
Mechanical Properties: A DCS - 5000 universal material testing equipment (Jinan Puye Electromechanical Technology Co., Ltd) was used to evaluate the compressive strength of the samples. The dimensions of the specimen material were 50 × 50 × 50 mm3. Every specimen underwent testing five times, and the arithmetic mean was calculated.
Thermal Conductivity Test: A TC3000 E thermal conductivity meter (produced by Xi’an Xiaxi Electronic Technology Co., Ltd) was employed to measure the thermal conductivity of the samples. Every specimen had a size of 50 × 50 × 25 mm3. Every specimen underwent testing three times, and the arithmetic mean was computed.
Thermogravimetric Analysis (TGA): The thermal stability of the samples (5-10 g) in a nitrogen atmosphere was studied using a DTG-60H thermogravimetric analyzer (Shimadzu, Japan). The analysis proceeded at a heating velocity of 20°C every minute, spanning a temperature range from ambient temperature to 800°C.
Cone Calorimeter Test (CCT): A VOUCH 6810 Cone Calorimeter (produced by Suzhou Yangyi Woerqi Testing Technology Co., Ltd) was employed to measure the combustion performance of the samples wrapped in aluminum foil in accordance with the ISO 5660-1 standard. Every specimen had a size of 100 × 100 × 25 mm3. The test was carried out under a radiant heat flux of 35 kW/m2 and an air flow rate of 24 L/s.
Scanning Electron Microscopy (SEM): The morphologies of the specimens and their carbonaceous residues were analyzed by virtue of a JSM - 6490LV scanning electron microscope (JEOL, Japan). The samples were subjected to surface conductive layer - spraying treatment before testing, and the acceleration voltage was 15 keV.
Laser Confocal Raman Spectroscopy (Raman): The specimens underwent heat treatment within a muffle furnace adjusted to a temperature of 600°C and maintained for 10 minutes to yield the carbon residue. During the examination of the carbon residues, a Lab. RAM HR Evolution (HORIBA Scientific) was utilized. The wavelength span was between 800 cm−1 and 2000 cm−1, and the resolution stood at 1 cm−1.
Fourier-Transform Infrared Spectroscopy (FTIR): Utilizing the Nicolet 6700 infrared spectrometer of Thermo Fisher Scientific from America, the FTIR spectra of the samples were obtained. The spectral range covered wavelengths from 4000 cm−1 to 400 cm−1, with a resolution of 4 cm−1.
Results and discussion
Characterization of OG sludge
Chemical composition of converter OG sludge.

XRD pattern of OG sludge.
Cell structure
The SEM was conducted to examine how OG sludge affects the cellular architecture of rigid polyurethane foam. As illustrated in Figure 2 (a), the original RPUF specimen exhibits a clear-cut closed-cell honeycomb configuration. There are small holes on certain parts of the honeycomb structures, and the overall cell size is relatively consistent. Figure 2 (b)-(d) show the cell structures of RPUF/OG sludge composites with different additions of OG sludge. As is evident from Figure 2, upon the addition of OG sludge, the cell size of the composite diminishes gradually. This may be because the addition of OG sludge reduces the free energy that is necessary for nucleation within the composite.
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At the same time, it was found that with the addition of OG sludge, the integrity and uniformity of the cells decline to some extent, leading to an increase in the proportion of open-cell structures. This issue might arise from the poor matching between the OG sludge particles and the cellular composition of the RPUF matrix.
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SEM images of RPUF and RPUF/OG composites: (a) RPUF; (b)RPUF/OG10; (c)RPUF/OG30; (d) RPUF/OG50.
Physical property
Physical properties of RPUF and RPUF/OG composites.
Combustion behavior and flame retardant properties
The CCT serves as a crucial testing approach for researching the combustion traits of polymer composites.46,47 CCT was applied to examine the heat release rate (HRR) and total heat release (THR) of RPUF and RPUF/OG composites. The curves of RPUF composites, along with the relevant data, are illustrated in Figure 3(a)-(b), and the relevant data are tabulated in Table 4. According to Table 4, the time to ignition (TTI) of RPUF, RPUF/OG10, and RPUF/OG30 are all between 1 and 3 s, which is chiefly associated with the organic substances and porous architecture of RPUF.
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However, the TTI of RPUF/OG50 reaches 9 s, mainly due to the following reasons. Firstly, with the increase in OG sludge addition, as a non - combustible component, OG sludge effectively reduces the RPUF content through the filler effect. Secondary, the tightly packed char layer that develops productively restrains the expulsion of flammable components produced by the cracking of RPUF. The peak heat release rate (PHRR) of RPUF reaches 410.5 kW·m−2. This implies that while the burning of RPUF is taking place, a significant amount of heat can be liberated, leading to severe thermal risks. As OG sludge is added, the PHRR of RPUF composites shows a gradual decline. Once the quantity of added OG sludge attains 50 parts, the PHRR descends to 342.9 kW·m−2, signifying a 16.5% reduction in comparison to RPUF. This demonstrates that the incorporation of OG sludge is advantageous for inhibiting the heat liberation during the combustion of the composite and enhancing its fire - safety characteristics. At the same time, it is found that OG sludge also has markedly decreases the THR of the composite material. As OG sludge increases, the THR of RPUF/OG composites slowly decreases. When 50 parts of OG sludge are added, the THR of the RPUF/OG50 composite drops to 23.3 MJ·m−2, a 24.1% decrease compared with the pure sample (30.7 MJ·m−2). The average effective heat of combustion (Av-EHC) reflects the combustion extent of volatiles in the gas phase during the combustion process.
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The Av-EHC value of the pure sample amounts to 137.38 MJ·kg−1. When 10 parts of OG sludge are added in, the Av-EHC of RPUF/OG10 descends to 60.86 MJ·kg−1, representing a 55.7% decrease relative to the pure sample. This demonstrates that OG sludge has a definite gas-phase flame retarding function. This is mainly because the metal oxide components contained in OG sludge have a certain quenching effect on H· and HO· gas phase radicals.
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(a) HRR, (b) THR, (c) SPR, (d) TSR, (e)Mass and (f) CO production curves of RPUF and RPUF/OG composites. Cone calorimeter data of RPUF and RPUF/OG composites.
Figure 3(c)-(f) illustrates the curves regarding the smoke release and mass of RPUF as well as RPUF/OG composites. As is evident from Figure 3(c), the smoke production rate (SPR) of the unadulterated sample reaches its peak (≈0.38 m2·s−1) 50 s after combustion, and then drops to zero at around 75 s. Upon the addition of OG sludge, the SPR of the RPUF/OG composites experiences a substantial reduction, and the addition of 50 parts of OG sludge is the most obvious, indicating that OG has obvious smoke - suppressing characteristics for RPUF/OG composites. This may be because the metal oxides within the OG sludge facilitate the aromatization and subsequent carbonization of the small molecule flammable constituents resulting from the thermolysis of the RPUF matrix, thereby decreasing the smoke particles discharged into the gas phase. Based on Figure 3(d), the total smoke release (TSR) for pure RPUF amounts to 654.1 m2·m−2, while the TSR of RPUF/OG50 reduces to 369.1 m2·m−2, signifying a 43.6% reduction relative to the unadulterated specimen. The smoke factor (SF) is the outcome of PHRR multiplied by TSR, providing a comprehensive measure of both heat release and smoke production. 50 As is also evident in Table 4, the SF of the pure specimen amounts to 2684.9 MW·m−2, and the SFs of RPUF/OG10, RPUF/OG30, and RPUF/OG50 are all significantly lower compared to the pure sample. Among these, the SF of RPUF/OG50 reduces to 1265.5 MW·m−2, signifying a 43.5% reduction when contrasted against the unadulterated specimen. The aforementioned results demonstrate that OG sludge exerts an outstanding smoke suppressing influence on RPUF composites. Figure 3(e) presents the variation in mass throughout the test. As is evident from the figure, upon the incorporation of OG sludge, the ultimate char yield of the RPUF composites exceed the pure specimen in this regard. The final char yield of the composite with 50 parts of OG sludge added is the largest, which amounts to 17.9 wt%, demonstrating that OG sludge is capable of enhancing steadiness of the RPUF composite when exposed to elevated temperatures. This outcome is in excellent agreement with the thermogravimetric test. Figure 3(f) presents the CO generation curves during the combustion of RPUF and RPUF/OG sludge composites. It is observable that pristine RPUF continuously generates CO during the combustion process, and the CO generation amount remains at 0.003 g·s−1 after 100 s until the end. After adding OG, the CO concentration of the RPUF/OG composite is equivalent to that of RPUF in the early stage. At around 130 s, its CO release amount rapidly decreases to 0.001 g·s−1. This can be ascribed to the fact that the low-valence Fe2+ in the OG sludge can promote the conversion of CO to CO2 during the combustion process through the oxidation reduction cycle. 51 The aforementioned data suggest that OG sludge can significantly decrease CO emissions while RPUF composites are burning and boost their fire safety characteristics.
On this basis, the Fire Growth Index (FGI) and Fire Performance Index (FPI) were introduced to quantitatively evaluate the impact of OG sludge on the fire safety of the composites. 4 FGI is formulated as the quotient of PHRR and the time needed to attain this peak value (Tp), whereas FPI is computed as the quotient of TTI and the PHRR. A greater FPI value and a reduced FGI value signify an improved level of fire safety for the composite material. As is shown in Table 4, the FPI and FGI of the pure sample are 0.0073 (m2·s)·kW−1 and 22.8 kW·(m2·s)−1, separately. Upon the addition of OG sludge, the FPI of the RPUF/OG composites shows a positive correlation with the quantity of added OG sludge, whereas the FGI exhibits a negative correlation with the amount of added OG sludge. Finally, the FPI of RPUF/OG50 is 0.0216 (m2·s)·kW−1 and the FGI is 20.17 kW·(m2·s) −1, indicating that OG sludge is capable of remarkably enhancing the fire safety of RPUF/OG composites.
LOI and UL-94 test results of RPUF and RPUF/OG composites.
Note: t1 and t2 represents the burning duration subsequent to the first and second ignition respectively; BC - burns to the clamp; NR - non rated.
Thermal stability
The TG and DTG curves of the RPUF/OG composites are presented in Figure 4. As can be seen from Figure 4 (a) (b), the thermal decomposition process of the RPUF composites mainly consists of two stages. The initial stage takes place in the temperature interval of 220 - 400°C and is related to the breakdown within the polyurethane molecular chain’s hard segments. During the second stage, one can observe the existence of the temperature region from 400 to 600°C, which is in line with the decomposition of the flexible components within the polyurethane molecular structure.
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In the case of the RPUF/OG30 and RPUF/OG50 composites, a third decomposition phase emerges at around 625°C. This phenomenon can be ascribed to the additional dehydration and stabilization of the char layer generated in the initial phase in high temperature environments, resulting in the formation of a more compact char layer.
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As presented in Table 6 for the pure RPUF composite, the temperature associated with a 5% reduction in mass (T-5%), the temperature associated with a 50% reduction in mass (T-50%), the peak temperature during the first stage decomposition (Tmax1), and the peak temperature during the second stage decomposition (Tmax2) are 253°C, 357°C, 355°C, and 620°C respectively. When 10 parts of OG sludge is added, the T-5% value of the RPUF/OG10 composite reaches a peak of 264°C, indicating that the incorporation of a minor quantity of OG sludge is capable of enhancing the thermal steadiness of the RPUF/OG composite. When the amount of OG sludge is increased further, the T-5% values of RPUF/OG30 and RPUF/OG50 are 248°C and 259°C, respectively. By contrast, the Tmax1 and Tmax2 values of the RPUF/OG composites exhibit no substantial alteration in comparison to those of the pure RPUF composite. This implies that the OG sludge primarily functions as a filler and does not engage in a chemical reaction in the RPUF matrix when at elevated temperatures.
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Nevertheless, as the amount of added OG sludge rises, the T - 50% value of the RPUF/OG composites gradually goes up. Additionally, the char yield at 800°C attains 21.7 wt%, being significantly superior to that of the unmodified RPUF composite. This suggests that OG sludge can significantly increase the steadiness of RPUF/OG composites under high-temperature conditions. (a) TG and (b) DTG curves of RPUF and RPUF/OG composites. TG and Cone calorimeter data of RPUF and RPUF/OG composites.
Carbon residue analysis
The SEM was utilized to explore the microscopic architecture of the carbon residues derived from RPUF composites following calcination in a muffle furnace. As is evident from Figure 5 (a), the carbon residue of the pure specimen features a substantial quantity of pore structures. The carbon layer is both thin and fragile, and such a structure fails to facilitate the reduction of heat transfer and the suppression of flame spread during combustion. From Figure 5 (b), it is noticeable that with the addition of 10 parts of OG sludge, the compactness of the carbon residue of RPUF/OG10 increases, and the pore structures are considerably decreased. When 30 parts of OG sludge are added, the thickness of the carbon layer of RPUF/OG30 is further increased, and more granular substances precipitate on its surface, as shown in Figure 5 (c). This is because during the combustion procedure, the OG sludge particles relocate to the outer layer of the carbon material. Consequently, the density of the carbon residue is increased, thereby inhibiting the transmission of heat and substances in the course of the composite’s combustion. Upon adding 50 parts of OG sludge, the carbon residue of RPUF/OG50 maintains the skeletal structure of RPUF during combustion, but its compactness decreases, as depicted in Figure 5 (d). SEM images and Raman spectra of RPUF and RPUF/OG composite carbon residue: (a),(e) RPUF; (b),(f) RPUF/OG10; (c),(g) RPUF/OG30; (d),(h) RPUF/OG50.
For a more in depth analysis of the char forming characteristics of RPUF and RPUF/OG composites, Raman spectroscopy was utilized to analyze the carbon residues of RPUF and RPUF/OG composites. As depicted in Figure 5(e)-(f), all curves exhibit a double peak pattern. The D peak, which is detected at around 1360 cm−1, is associated with non-crystalline carbon atoms. In contrast, the G peak, identified at about 1580 cm−1 has a connection with carbon atoms in the crystalline phase. 5 The ratio of the peak areas of the D peak to the G peak (ID/IG) serves to depict the degree of graphitization in carbon materials. A decreased ID/IG ratio implies a greater level of graphitization within the carbon residue, resulting in superior heat-resistant properties. The ID/IG ratio of the unadulterated sample is 2.33. With the addition of OG sludge, the ID/IG value of the RPUF/OG composites decreases, indicating that the metal oxides present in OG are capable of facilitating the carbonization and graphitization processes of the polyurethane molecular chain. Once 30 parts of OG sludge are incorporated, the ID/IG value of the carbonaceous residue in RPUF/OG30 decreases further to 2.01. This implies that the addition of a suitable quantity of OG sludge is capable of facilitating the generation of a graphitized carbon stratum inside the RPUF matrix. When the amount of OG sludge added reaches 50 parts, the ID/IG value rises to 2.07 again, indicating that the addition of an excessive amount of OG sludge is not conducive to the graphitization process of the RPUF matrix.
Mechanisms of flame retardation and smoke suppression
As a result of the aforesaid analysis, the mechanism by which the RPUF/OG composite retards flames is described in Figure 6. It can be concluded that the OG sludge exerts its effect mainly through the following ways: Firstly, it can reduce the content of RPUF through the filler effect, thereby reducing the combustibility of the RPUF composite. Secondly, the metal oxides within the OG sludge are capable of facilitating the carbonization and graphitization of the decomposition products of the polyurethane molecular chain. They augment the density of the carbonaceous layer and efficiently impede the exchange of substances and heat in the course of the combustion process. Thirdly, the metal oxides within the OG sludge are able to scavenge HO· and H· in the gas phase, thereby attaining the goal of gas phase flame retardancy.
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Therefore, the OG sludge demonstrates its flame retardant effect primarily through the synergistic mechanism between the gas and condensed phases. Diagram illustrating the flame retardant mechanism of RPUF/OG composites.
Conclusion
To address the dual challenges of environmental pressure from metallurgical solid waste OG sludge and the high flammability of RPUF, this study innovatively utilized OG sludge as a flame retardant additive and successfully prepared RPUF/OG composites via a one-step all-water foaming technique. The effects of OG sludge content on the thermal stability, combustion performance, char residue morphology, and graphitization degree of RPUF/OG were systematically investigated. The research demonstrates that the incorporation of OG sludge effectively enhances the overall fire safety performance of the composites. Although the improvement in the LOI is limited, it significantly suppresses dripping and slows down flame spread. CCT indicate that the peak heat release rate of the RPUF/OG composites decreases with the addition of OG sludge, and the time to peak is advanced. When the OG sludge content reaches 50 parts, the PHRR and TSR of the RPUF/OG50 composite are reduced by 16.5% and 43.6%, respectively, compared to pure RPUF. This result clearly indicates that OG sludge effectively suppresses both the fire intensity and smoke production of the composites. TG reveals that the addition of OG sludge primarily functions in the condensed phase through a physical filling mechanism. While it does not alter the main thermal degradation pathway of the RPUF matrix, it significantly enhances the high temperature stability and char forming ability of the material. The residual char yield of the RPUF/OG50 composite at 800°C increases to 21.7 wt%, effectively improving the high-temperature stability of the RPUF/OG composites and forming a more stable protective barrier. SEM and Raman spectroscopy results of the char residues indicate that an appropriate amount of OG sludge can guide the formation of a denser, more highly graphitized protective char layer, thereby effectively inhibiting heat transfer during combustion. However, excessive addition can compromise char layer integrity due to filler agglomeration. This work opens a new pathway for the high-value resource utilization of metallurgical process solid waste OG sludge and provides insights for enhancing the fire safety performance of RPUF building insulation materials.
Footnotes
Acknowledgements
This research was supported by National Natural Science Foundation of China (No.22075053), the Natural Science Foundation of the Anhui Higher Education Institutions (No.2022AH050288), Anhui Student Research Training Program (No.S202310360230), Anhui Provincial Nature Science Foundation (No.2108085ME178), Anhui Province Key Laboratory of Environment-friendly Polymer Materials (No.KF-202307).
Author contributions
Yani Zhang: Conceptualization; Data curation; Formal analysis; Investigation; Methodology; Writing - original draft. Zhen Dai: Data curation; Formal analysis; Investigation; Writing – original draft. Xunyi Wang: Data curation; Funding acquisition; Investigation; Writing - review & editing. Xinjie Huang: Funding acquisition; Investigation; Supervision; Formal analysis. Zimin Liu: Formal analysis; Project administration; Supervision; Writing - review & editing. Qiang Wu: Writing - review & editing, Formal analysis, Supervision. Kang Dai: Supervision; Writing - review & editing; Funding acquisition. Xiuyu Liu:Writing - review & editing; Funding acquisition. Gang Tang: Supervision, Project administration, Writing - review & editing; Funding acquisition; Methodology.
Declaration of conflicting interests
The authors declare that they have no known competing financial interests or personal relation-ships that could have appeared to influence the work reported in this paper.
Funding
The authors disclosed receipt of the following financial support for the research, authorship, and/or publication of this article: This research was supported by National Natural Science Foundation of China (No.22075053), the Natural Science Foundation of the Anhui Higher Education Institutions (No.2022AH050288), Anhui Student Research Training Program (No.S202310360230), Anhui Provincial Nature Science Foundation (No.2108085ME178), Anhui Province Key Laboratory of Environment-friendly Polymer Materials (No.KF-202307).
Data Availability Statement
The data that support the findings of this study are available from the corresponding author, upon reasonable request.
