Home Journals Articles Updates About
CN
image
收藏切换
Investigating the migration mechanisms of heavy metals under silicate polymerization in gasification slag from landfilled municipal solid waste with rice husk addition
收藏切换
PDF
Qinwei HUANG, Longfei TANG*, Xia LIU, Weitong PAN, Xueli CHEN*, Fuchen WANG
Journal of Fuel Chemistry and Technology | 2026, 54(7) : 20250285-1348 - 20250285-1362
Less
收藏切换
Journal of Fuel Chemistry and Technology | 2026, 54(7): 20250285-1348-20250285-1362
• RESEARCH PAPER •
Investigating the migration mechanisms of heavy metals under silicate polymerization in gasification slag from landfilled municipal solid waste with rice husk addition
Full
Qinwei HUANG, Longfei TANG*, Xia LIU, Weitong PAN, Xueli CHEN*, Fuchen WANG
Affiliations
  • Institute of Clean Coal Technology, East China University of Science and Technology, Shanghai 200237, China
Published: 2026-07-10 doi: 10.1016/S1872-5813(26)60676-7
Outline
收藏切换

Slag gasification represents one of the key technologies for the clean and resource-oriented treatment of organic solid wastes with high heavy-metal content, such as landfilled municipal solid waste. Using rice husk as a silicon source, this work investigated the effect of rice-husk addition on the vitrification of landfilled-waste slag and the solidification behavior of heavy metals. The results demonstrated that the incorporation of rice husk (5%−10%) lowered the flow temperature of the slag and effectively suppressed heavy-metal leaching. Specifically, the leaching concentrations of Cr and Zn decreased from 41.60 and 108.00 mg/L to 5.89 and 7.10 mg/L, respectively. The active SiO2 introduced by rice husk promoted the formation of highly polymerized siloxane networks (Q3, Q4), which inhibited gasification-induced migration of heavy metals and enhanced physical encapsulation of them. Concurrently, it facilitated the incorporation of Zn2+, Cr3+ and Cu2+ via substitution or solid-solution mechanisms into stable mineral phases such as Zn2SiO4 and CuFe2O4, immobilizing them in garnet and spinel structures. This process increased the residual fraction and reduced the bioavailability of the heavy metals. The present study elucidates the mechanistic role of rice husk in modulating slag structure and heavy-metal immobilization, thereby provides a theoretical basis for the clean and efficient co-treatment of landfilled waste and biomass through a “treating waste with waste” strategy.

landfilled municipal solid waste  /  rice husk  /  heavy metal immobilization  /  gasification slag  /  ash slag
黄钦威, 唐龙飞, 刘霞, 潘伟童, 陈雪莉, 王辅臣. 稻壳对填埋生活垃圾气化熔渣中硅酸盐聚合作用下重金属迁移机制研究. 燃料化学学报（中英文）, 2026 , 54 (7) : 20250285-1348 -20250285-1362 . DOI: 10.1016/S1872-5813(26)60676-7
Qinwei HUANG, Longfei TANG, Xia LIU, Weitong PAN, Xueli CHEN, Fuchen WANG. Investigating the migration mechanisms of heavy metals under silicate polymerization in gasification slag from landfilled municipal solid waste with rice husk addition[J]. Journal of Fuel Chemistry and Technology, 2026 , 54 (7) : 20250285-1348 -20250285-1362 . DOI: 10.1016/S1872-5813(26)60676-7
Full Text
Less
Over the past 40 years of reform and opening-up, the historically stockpiled landfilled municipal solid waste (MSW) in China has exceeded 8 billion tons[1]. Its high moisture content (30%−50%)[2], high ash content (>50%), and complex speciation of heavy metals[3] make it difficult for traditional incineration-landfill coupling processes to achieve waste reduction, harmless treatment, and resource recovery simultaneously. Pre-treated (sun-dried and screened) landfilled waste exhibits a calorific value of approximately 18−29 MJ/kg[4], which is comparable to that of coal[5]. The overall thermal efficiency during gasification exceeds 75%[6], rendering MSW suitable as a feedstock for gasification. The application of waste gasification technology to process the vast stockpile of landfilled waste with complex composition enables the complete resource recovery of waste[7]. This not only provides a novel approach to addressing environmental issues but also opens new pathways for developing alternative energy sources.
The composition of municipal solid waste is complex, with common waste items such as spent batteries, electronic products, paints, and cosmetics containing heavy metals[8]. Heavy metals are generally defined as metallic elements with a density >4.5 g/cm3. Elements such as mercury (Hg), cadmium (Cd), chromium (Cr), nickel (Ni), copper (Cu), lead (Pb) and zinc (Zn) emitted from MSW incineration plants are classified as heavy metals[9]. It is widely acknowledged that the heavy metal content in waste tends to increase with landfill age[10]. During the collection, transportation, and treatment of waste, heavy metals migrate and transform via physical transport, chemical dissolution, and biological leaching[11]. Their migration and transformation during incineration follow an evaporation-condensation mechanism[12]. Slagging gasification, a treatment technology capable of simultaneously achieving vitrification of organic solid waste ash and efficient resource recovery[13], converts waste into syngas (H2/CO) at high temperatures (>1200 °C). The resulting slag possesses vitreous characteristics, offering the dual advantages of nearly complete dioxin decomposition (>99.9%) and physical encapsulation of heavy metals[14].
Studies indicate that the chemical composition of slag derived from landfilled MSW is typically dominated by CaO and SiO2. However, a high content of alkaline oxides (e.g., CaO, MgO) can disrupt the three-dimensional silicate network structure, leading to an increased degree of slag polymerization (indicated by a higher NBO/T ratio) and reduced viscosity. If the SiO2 content in the slag is insufficient or the alkaline component content is excessive, the silicate network struggles to form a stable vitreous structure[15]. The migration of heavy metals during the melting process is jointly controlled by temperature, atmosphere, and the silicate-oxygen structure of the slag[16]. As shown in Table 1, heavy metals exist in diverse speciations. Volatile elements such as Pb, Zn and Cd tend to release as chlorides within 1000−1200 °C range[17], whereas Cr, Ni and Cu predominantly remain in the slag as oxides[18]. Consequently, the risk of heavy metal re-release from the slag and the insufficient degree of silicate network polymerization remain the core bottlenecks hindering its engineering application. Furthermore, the complex composition of landfilled waste and significant fluctuations in ash composition[19] result in inherently low SiO2 content (<30%). This leads to a low degree of polymerization of the [SiO4]4− tetrahedra in the slag, causing breaks in the silicate chains and the formation of non-bridging oxygen atoms, which in turn provides weak binding sites for heavy metals.
Biomass addition can improve slag performance through a triple mechanism involving thermochemical conditioning, provision of a reducing atmosphere, and supplementation of silicon sources. Among various agricultural wastes, rice husk, a by-product of rice processing with an annual global output exceeding 120 million tons[21], is also a significant component of the actual discharge of township MSW[22] and is typically regarded as a low-value waste[23]. However, rice husk possesses a large specific surface area[24] capable of capturing heavy metal ions via physical adsorption[25]. Its ash contains >90% amorphous SiO2[26] and abundant silanol groups[27], making it an ideal active SiO2 source. It reacts with CaO and Al2O3 present in the landfilled waste, regulating silicate phase transformation and network reconstruction[28] during heat treatment to form highly polymerized Q3 and Q4 siloxane structures (Si−O−Si). Surface oxygen-containing functional groups of rice husk-derived biochar can undergo chemical reactions with heavy metal ions, forming stable surface complexes[29]. Acting as a fluxing agent[30], it facilitates the formation of a dense vitreous network structure[31]. Theoretically, this dual mechanism of “structural encapsulation” and “chemical bonding” can enhance heavy metal immobilization[32]. However, excessive rice husk may reduce slag basicity, thereby inhibiting silicate reconstruction and exacerbating heavy metal volatilization. Currently, the coupling relationships among the rice husk blending ratio, melting temperature, and heavy metal immobilization efficiency, along with the microscopic regulatory mechanisms governing silicate polymerization behavior, remain critical scientific questions requiring breakthroughs in this field.
Given the current situation that landfill capacities are nearly exhausted and siting new landfills is challenging, a gap still remains in the comprehensive treatment of landfilled waste. This study focuses on the gasification of the typical landfilled MSW. By regulating the rice husk blending ratio (0−20%) and the melting temperature (1300−1500 °C), the migration patterns of typical heavy metal elements (Zn, Cr, Cu) in the gas-slag phases were systematically investigated. Methods such as XRD, Raman spectroscopy, and FT-IR are employed to analyze the evolution of the degree of silicate network polymerization (NBO/T ratio, Qn distribution). The study aims to explore the correlation mechanism among rice husk blending, silicate structure, and heavy metal immobilization efficiency. The objective is to provide a theoretical basis for resource utilization and heavy metal risk control in the slagging gasification process of landfilled waste with rice husk, while also to offer new insights for the thorough remediation of landfill hazards via the principle of “using waste to treat waste.”
1　Experimental
Less
1.1　Experimental materials
Landfilled municipal solid waste (MSW), collected from a river remediation project in Qingpu District, Shanghai, with a landfill age of approximately 15 years, was used as the primary research object and labeled as QP. It primarily consisted of 67.15% plastics and rubber, 21.21% textiles, and 8.94% wood/bamboo, among other components. Compared to other MSW[33], QP had a higher content of plastics and rubber, exhibiting characteristics similar to landfills both domestically and internationally, predominantly featuring humus soil mixed with plastics[34]. Rice husk specimens were collected from fresh seasonal harvests in the Northeast region. The husks were dried at 60 °C for 5 h, subsequently pulverized and sieved to isolate particles within the 100−120 mesh size range.
Following standards CJ/T 313—2009, the waste underwent collection, sorting, crushing, washing, and drying. Its physical composition is shown in Figure 1. In accordance with national standards GB/T 212—2008 and GB/T 476—2008, proximate analysis, ultimate analysis, and calorific value analysis were performed on two raw materials: freshly harvested rice husk (DK) from Northeast China and the landfilled waste (QP). The analyses were conducted using a Changsha Kaiyuan 5E-MACⅢ infrared rapid coal analyzer, a Vario MACRO elemental analyzer, and an oxygen bomb calorimeter. The results are presented in Table 2. The rice husk exhibited relatively high ash and volatile matter contents of 14.56% and 67.52%, respectively, aligning with the typical characteristics of agricultural and forestry biomass ash[35].
The QP sample showed ash and volatile matter contents of 20.17% and 75.86%, respectively, approaching the ash composition of lignite[36]. As plastics are the key factor determining the calorific value of waste, this sample exhibited a relatively high calorific value[37]. Additionally, the chlorine content of QP was determined to be 1.15%, which is considered a high level[38].
QP was placed in a muffle furnace, and programmed temperature ashing was performed following standard GB/T 28731—2012: initially, the temperature was raised from room temperature to 30 °C within 10 min; subsequently heated to 250 °C over 50 min and held for 60 min; then heated to 550 °C over 60 min and maintained at that temperature for 2 h. After sample preparation via pelletizing, the chemical composition of the QP ash was determined using X-ray fluorescence spectrometry.
To investigate the immobilization effect of minerals in the low-temperature melting zone (Figure 2) on Cu, Zn and Cr, fresh rice husk samples were mixed with QP at weight ratios of 5%, 10%, 15% and 20% to achieve different primary mineral phases at high temperatures. The five samples with varying rice husk additions were labeled DK00, DK05, DK10, DK15 and DK20, respectively. Their chemical compositions are shown in Table 3. The highest component in all five ash samples was SiO2, with its content significantly increasing as the rice husk addition ratio increased. Contents of CaO, Fe2O3 and MgO continuously decreased, while that of Al2O3,K2O and Na2O changed gradually. The content of Cl and SO3 showed fluctuations. The silicon-to-aluminum ratio (S/A) of QP was relatively high at 3.08, consistent with the characteristics of typical MSW ash.
As shown in Figure 2, DK00 (without rice husk addition) is located near the boundary between dicalcium silicate and calcium silicate. With increasing rice husk addition, its composition gradually shifts towards the upper right.
1.2　Slag sample preparation
To obtain quenched slag samples required for analyzing mineral composition at specific temperatures, a measured mass of ahs sample was placed in a corundum crucible. A CO2 flow rate of 200 mL/min and a CO flow rate of 300 mL/min were set to ensure a weakly reducing atmosphere[39] during the experiment. The crucible was pushed into the heating zone of the furnace at 1200 °C, then heated to the specified temperature at a rate of 5 °C/min. It was held at 1300, 1400 and 1500 °C for 5 min each, then rapidly removed and quenched with liquid nitrogen. After cooling, the bottom of the corundum crucible was cut off, and the slag was chiseled out with a hammer and ground to a particle size of less than 100 μm for characterizations.
1.3　Sample analysis
After ball milling, the mineral composition of the ash/slag was analyzed using a Dutch PANalytical D/MAX2550-VB/PC XRD instrument (Cu target, 40 kV/40 mA, scanning range 10°−80°) combined with Jade 6.5 software. Following standard GB/T 219—2008, ash fusibility characteristic temperatures (DT, ST, HT, FT)[40] were determined under a weakly reducing atmosphere using a Changsha Kaiyuan 5E-AFIII ash fusion temperature tester. Thermodynamic simulations of the SiO2-Al2O3-CaO-Fe2O3-MgO-K2O-TiO2-Na2O system from 800−1500 °C (at 50 °C intervals) were performed using FactSage software to predict mineral phase evolution and solid/liquid phase content. The network structure of the slag quenched at 1400 °C was characterized by Fourier Transform Infrared Spectroscopy (FT-IR, Nicolet iS50, KBr pellet method, 4000−400 cm−1, resolution 1 cm−1) and Raman spectroscopy (Thermo Fisher Scientific instrument, 455 nm laser/3 mW, 300−1300 cm−1, resolution 1 cm−1, PeakFit Gaussian fitting). Additionally, the micro-morphology and elemental distribution of the ash/slag were analyzed using a Hitachi SU-1510 SEM-EDS.
1.4　Quantitative analysis method for heavy metals
Based on USEPA Method 29, heavy metal content in ash samples was determined using a microwave digestion and ICP-MS. Approximately 0.1 g of sample was weighed into a polytetrafluoroethylene digestion vessel, followed by the addition of 4 mL concentrated nitric acid. Microwave digestion was performed at 280 °C until the solution became clear. The digestion vessel was then placed on a 150 °C graphite hotplate for acid evaporation until 1.0 − 2.0 mL remained. After cooling, the solution was transferred to a 50 mL volumetric flask and diluted to the mark with distilled water. Heavy metal concentrations in the digestate were analyzed using ICP-MS.
The enrichment and retention characteristics of heavy metals in the slag were characterized by the Enrichment Ratio (ER) and Retention Ratio (RR), with the volatilized portion in the gas phase represented by the Volatilization Rate (1-RR). The yield of ash converted to slag is defined as Y, and the weight loss rate (1-Y) is the percentage mass loss during the ash heating process. The calculation formulas are as follows:
$ {\mathrm{ER}}=\frac{{C}_{x}}{C} $
$ Y=\frac{{m}_{x}}{m}\times 100\% $
$ {\mathrm{RR}}=\frac{{C}_{x}{m}_{x}}{Cm}={\mathrm{ER}}\times Y $
where Cx is the heavy metal concentration in the slag (mg/kg); C is the heavy metal concentration in the ash (mg/kg); Y is the yield of ash converted to slag (%); mx is the mass of the slag sample after melting (g); m is the mass of the ash before melting (g).
1.5　Solid leaching toxicity analysis
The solid leaching toxicity analysis was conducted according to the GB 16889—2008 standard (using the HJ/T 300—2007 acetic acid buffer solution method). The corresponding ash/slag samples were dried at 105 °C for 2 h to determine moisture content (Note: These dried samples were not used for the leaching experiment). Leachant selection: 5 g of sample was weighed, mixed with 96.5 mL of pure water, and stirred for 5 min to measure pH. If pH < 5, leachant #1 was used (5.7 mL glacial acetic acid + 64.3 mL 1 mol/L NaOH diluted to 1 L, pH = 4.93±0.05). If pH > 5, 3.5 mL of 1 mol/L hydrochloric acid was added, heated at 50 °C for 10 min, and pH was measured again. If pH < 5, leachant #1 was used; otherwise, leachant #2 was used (17.25 mL glacial acetic acid diluted to 1 L, pH = 2.64±0.05). Leachant #1 was used in this experiment. The leachant was added at a liquid-to-solid ratio of 20∶1 based on the moisture content, followed by end-over-end agitation (30±2 r/min, 18±2 h). After standing for 20 min, the mixture was vacuum-filtered through a 0.45 μm membrane filter. The filtrate was treated with 4−5 drops of 1∶1 nitric acid and stored refrigerated. Heavy metal concentrations in the leachate were determined using ICP-MS and compared against the limit standards of GB16889—2008.
2　Results and discussion
Less
2.1　Effect of rice husk addition on the ash fusion behavior of landfilled municipal solid waste
The ash fusion temperatures of the mixed samples are related to the amount of the same biomass added[41]. Since rice husk itself is a lightweight biomass with low density and large volume, an excessively small blending amount can easily lead to uneven combustion[42]. Therefore, an incremental addition of 5% for investigation was employed in this study. Figure 3 shows the ash fusion temperatures of samples with different proportions of rice husk addition under a weakly reducing atmosphere. It can be seen from the figure that as the proportion of rice husk increases, DT, ST, HT and FT are all lower than those of the original sample. FT shows a trend of first decreasing and then increasing, while DT, ST and HT show a more pronounced decrease at 5% and 10%. DK05 exhibits the lowest values for all four fusion characteristic temperatures, with an FT of 1213 °C. Combined with Table 3, the SiO2 introduced by 5% addition of rice husk reacts with the abundant CaO, Fe2O3 and K2O in the waste ash, forming low-melting eutectic phases such as anorthite (CaAl2Si2O8) and KCl/K2SO4, significantly lowering the initial melting temperature. When the addition ratio exceeds 15%, an increase in melting point occurs. This is attributed to an excessively high silicon-to-aluminum ratio, causing low-melting silicates like anorthite to form a viscous liquid at high temperatures, hindering ash flow and leading to secondary slagging[43]. Additionally, SiO2 forms a high-melting quartz phase (melting point 1713 °C), diluting the flux concentration. Meanwhile, the absolute amount of alkaline oxides decreases, which is insufficient to generate an adequate amount of low-temperature eutectic melt.
Thermodynamic simulations calculated the solid and liquid phase fractions and mineral compositions of the five ash samples under equilibrium conditions from 800−1500 °C in a weakly reducing atmosphere, with results shown in Figure 4.
The results indicate that DK05 contains KCaCl3 and FeS chloride/sulfide eutectics at 800 °C, which can lower the DT. At 1150 °C, the co-melting of anorthite and fayalite causes the molten slag phase to surge to 71.98%, contributing to a lower fusion temperature. For DK00, perovskite with high-melting point remains stable before 1100 °C. At 1200 °C, pyroxene/anorthite still dominate, and due to the relatively high CaO content, it reacts with SiO2 to form high-melting wollastonite (CaSiO3). For DK20 and DK15, the flux concentration is diluted due to their excess SiO2. The higher amount of free SiO2 and the high-melting quartz network hinder the expansion of the low-temperature melt[44].
The XRD patterns of the five samples after co-combustion are shown in Figure 5. It can be seen that the minerals contained in the DK00 sample include quartz (SiO2), calcite (CaCO3), plagioclase (Ca2Al2SiO7), perovskite (CaTiO3), etc. As the proportion of rice husk increases, the diffraction peaks of other crystals besides SiO2 decrease significantly. Both plagioclase (Ca2Al2SiO7) and perovskite (CaTiO3) have relatively high melting points, which is the reason for the higher ash fusion temperatures observed in Figure 3. As shown in Figure 6, when the temperature reaches 1400 °C, the slags are completely molten because it exceeds the flow temperatures of all five slags. It can be clearly observed that the slags are predominantly amorphous substances, but high-melting silicate minerals such as spinel, cordierite, and åkermanite still exist.
2.2　Effect of rice husk addition on heavy metal distribution in ash/slag from landfilled municipal solid waste
Heavy metal elements migrate to varying degrees during the combustion of landfilled waste and become enriched in the ash/slag. To better understand the enrichment characteristics of heavy metal elements in the solid-phase products, the Relative Enrichment Factor (Re)[45] is introduced for evaluation. Its expression is:
$ {\mathrm{Re}}=\frac{{C}_{{\mathrm{ash,}i}}\times {A}_{{\mathrm{d}}}}{{C}_{{\mathrm{QP,}i}}} $
where Cash,i represents the mass concentration of heavy metal element i in the ash/slag (mg/kg); CQP,i represents the mass concentration of heavy metal element i in the raw waste sample (mg/kg); Ad represents the ash content (as received basis) of the raw sample (%). Here, i represents heavy metal elements Pb, Cd, Cr, Zn, Cu, Hg, As. The contents of several heavy metal elements and their relative enrichment factors are shown in Table 4. Cu and Zn have higher contents due to their widespread pollution sources [46], while others such as Pb, Cd, Cr, As also have certain contents in the raw material and ash. Due to its low proportion in the overall waste and high volatility, Hg content in ash is extremely low. Benefiting from the high-temperature slagging gasification technology, some heavy metal elements have already formed stable mineral phases[47] with silicates, aluminates, or iron oxides in the ash/slag during high-temperature combustion. The relative enrichment factors in the ash/slag follow the order: As < Zn < Cr < Cu < 1.
Table 5 presents the heavy metal leaching toxicity of the five ash/slag samples. It can be found that after adding rice husk, the heavy metal leaching concentrations are all lower than those of the original sample, with DK05 showing the greatest reduction. Since the leaching concentrations of heavy metals such as As, Cd and Hg are extremely low and it is lack of statistically significant differences, the three high-content heavy metal elements: Cr, Cu and Zn were focused in this study. Through three sets (A, B, C) of melting experiments (QP ash with different rice husk ratios, melted at 1300, 1400 and 1500 °C, respectively), the heavy metal content in the slags was detected to explore the effects of melting temperature and rice husk addition on the enrichment and retention behavior of heavy metals in the ash/slag.
Since increasing temperature promotes the migration of heavy metals to the gas phase[48], the temperature range with a high weight loss rate usually corresponds to the peak of heavy metal volatilization[49]. As shown in Figure 7, when the melting temperature is constant, the weight loss rate ranges between 12%−19%, and it decreases as the rice husk addition ratio increases. When the rice husk addition ratio is the same, the difference in weight loss rate at different melting temperatures is relatively small. The high weight loss rate at high temperatures can promote the vitrification of ash/slag, encapsulating heavy metals within the aluminosilicate matrix and reducing leaching toxicity[50]. This indicates that compared to melting temperature, the rice husk content has a greater influence on the ash weight loss rate, and rice husk promotes the vitrification of the ash/slag.
The Enrichment Rate (ER) characterizes the degree of heavy metal enrichment in the slag[37], reflecting the relative relationship between its volatilization and mass loss. The results in Figure 8 show that for Cu and Zn elements, when the rice husk addition ratio is fixed, ER decreases with increasing melting temperature. When the melting temperature is fixed, ER increases with increasing rice husk addition ratio. The enrichment rate of Cu mainly fluctuates between 0.4−0.75, and that of Zn mainly between 0.37−0.69. For the Cr element, there is no significant correlation with either the rice husk ratio nor the melting temperature. Due to its high boiling point[51] and stable chemical forms[52], enrichment rate of Cr mainly fluctuates around 1.1. Under the same conditions, the enrichment intensity sequence is: Cr > Cu > Zn.
The Residual Rate (RR) characterizes the retention amount of heavy metals in the slag after high-temperature treatment[53], reflecting their distribution between the solid and gas phases. Figure 9 shows the RR of Cu, Cr and Zn in the slag under different melting temperatures and rice husk addition ratios. The RR of Cu and Zn elements increases with higher rice husk addition ratios and decreases with higher temperatures. At the same rice husk addition ratio, RR changes little with temperature, indicating that rice husk content has a greater influence on RR than melting temperature.
The RR of Cr shows no significant association with either the rice husk ratio nor the melting temperature. The RR ranges for Cu, Zn and Cr are 32%−65%, 30%−58% and 70%−123%, respectively. The distribution of RR range is related to elemental properties. Cu and Zn have good thermal stability and low volatility, while Cr tends to convert into stable oxides and is difficult to volatilize[54], therefore, all three elements are mainly present in the solid-phase slag.
As shown in Figure 10, thermodynamic simulation calculations revealthat the Cr element tends to be immobilized in garnet (Ca3Cr2Si3O12) during low-temperature processes and tends to be effectively immobilized in the slag through the formation of spinel phases (e.g., MgAl2O4, MgCr2O4, FeCr2O4) at high temperatures. The concentration of gaseous CrCl2 is low, indicating that most Cr is immobilized, which is consistent with the XRD analysis results. The Cu element mainly volatilizes in the form of gaseous CuCl, but the introduction of rice husk significantly reduces its gas-phase concentration, indicating that rice husk has a positive effect on inhibiting copper volatilization. In contrast, the behavior of Zn is relatively more complex. A low proportion of rice husk can suppress its volatilization to some extent, and Zn is immobilized by entering spinels. However, when the addition ratio exceeds 10%, due to the introduction of potassium elements, it promotes the formation of gaseous double salt chlorides like KZnCl3/NaZnCl3, weakening part of immobilization ability of Zn in silicate minerals such as melilite. The SiO2-rich rice husk ash reacts with heavy metal oxides or chlorides to form relatively stable silicate compounds. Relevant reaction formulas are shown below:
$ \mathrm{Cr}_{ \mathrm{2}} \mathrm{O}_{ \mathrm{3}} \mathrm{+MgO \to MgCr}_{ \mathrm{2}} \mathrm{O}_{ \mathrm{4}} $
$ \mathrm{3CaO+Cr}_{ \mathrm{2}} \mathrm{O}_{ \mathrm{3}} \mathrm{+3SiO}_{ \mathrm{2}} \mathrm{\to Ca}_{ \mathrm{3}} \mathrm{Cr}_{ \mathrm{2}} \mathrm{Si}_{ \mathrm{3}} \mathrm{O}_{ \mathrm{12}} $
$ \mathrm{4Cu+O}_{ \mathrm{2}} \mathrm{\to 2Cu}_{ \mathrm{2}} \mathrm{O} $
$ \mathrm{2CaO+ZnO+2SiO}_{ \mathrm{2}} \mathrm{\to Ca}_{ \mathrm{2}} \mathrm{ZnSi}_{ \mathrm{2}} \mathrm{O}_{ \mathrm{7}} $
$ \mathrm{ZnO+Fe}_{ \mathrm{2}} \mathrm{O}_{ \mathrm{3}} \mathrm{\to ZnFe}_{ \mathrm{2}} \mathrm{O}_{ \mathrm{4}} $
The speciation distribution of heavy metals determines their ecological toxicity, and different occurrence forms of heavy metals bring different environmental impacts. According to the BCR method[55], heavy metals are generally divided into acid-soluble fraction (F1), reducible fraction (F2), oxidizable fraction (F3) and residual fraction (F4). As shown in Figure 11, in the original ash, the occurrence forms of Cu, Zn, and Cr are all dominated by the acid-soluble fraction (F1), but there are some differences. The acid-soluble and reducible fractions are considered bioavailable because they can easily release into the environment[56], hence called bioavailable forms.
High-temperature treatment promotes the transformation of heavy metals into the residual fraction[57], which is stable in nature and difficult for organisms to utilize[58]. As the proportion of added rice husk increases, Cu, Zn and Cr all exhibit a certain degree of bioavailability and toxicity, but the residual fraction increases for all. The residual fraction is stable and not easily utilized by organisms. It can be seen that the immobilization effect is improved most significantly for Cr. For Cr, the proportion of its residual fraction (F4) continuously increases from 32.9% in the original sample to 61.8% at 20% blending ratio. This is mainly attributed to the similar ionic radii of Cr3+ and Si4+, allowing Cr3+ to be efficiently immobilized via isomorphism into the newly formed silicate glass network structure. The growth of the residual fraction proportion for Zn is slow when the blending ratio is between 5%−15%, which is attributed to the dilution of fluxes (Fe2O3, Al2O3), weakening the formation of spinel phases like zinc ferrite. Whenrice husk addition reaches 20%, the formation of the more stable willemite (Zn2SiO4) becomes dominant, leading to a significant increase in the residual fraction. The speciation distribution of copper is obviously affected by the competitive interference of chlorine. At the chlorine content peak (DK15, 4.26%), the proportion of the residual fraction for copper shows a decline, indicating that the volatilization-recondensation process of gaseous CuCl2 leads to the enrichment of active forms. Combined with the previous leaching concentration analysis, when the addition amount of rice husk is 20%, the leaching concentrations of some heavy metals increase. This should be due to the excessive dilution of CaO and Fe2O3 content, leading to insufficient formation of garnet and spinel phases. Excess Cr cannot be effectively immobilized in the slag, and the reduced alkalinity weakens the ability to immobilize chlorine, interfering with the speciation of Cu. However, the leaching concentrations of Zn and Cr still show a decrease at the 20% addition level. Based on this finding, the immobilization mechanism of physical encapsulation was further explored.
2.3　Mechanism analysis of heavy metal immobilization in slag by rice husk addition
The core of the slag structure is the network polymer structure composed of silicon-oxygen tetrahedra[59]. To deeply explore the microscopic mechanism of heavy metal immobilization enhanced by rice husk, FT-IR and Raman spectroscopy were employed to analyze the silicate network structure of the slag[60]. FT-IR was used to characterize the degree of polymerization in the liquid phase of the five samples at 1400 °C. The strongest absorption band in the 800−1300 cm−1 range corresponds to the symmetric stretching vibration of Si−O. The polymerization degree of the [SiO4] tetrahedral units is represented by Qn, where n is the number of bridging oxygens (Si−O−Si) and reflects the degree of liquid phase polymerization. Q0, Q1, Q2, Q3 and Q4 correspond to monomers ([SiO4]4−, Q0), dimers ([Si2O7]6−, Q1), sheet structures ([SiO3]2−, Q2), network structures ([Si2O5]2−, Q3), and three-dimensional networks (SiO2, Q4), respectively. The characteristic wavenumber ranges for Q0−Q4 are 840−890, 900−950, 960−1030, 1050−1100 and 1060−1190 cm−1, respectively. Peaks between 800−1300 cm−1 were deconvoluted using Gaussian functions, where the proportion of Qn is linearly related to the characteristic peak area. Table 6 lists the characteristic structures involved in peak fitting and their center positions. The ratio（Q0+Q1+Q2）/（Q3+Q4）(denoted as R) is defined as an evaluation index for liquid phase polymerization degree[61]. A decrease in the R value indicates polymerization has occurred in the liquid phase. Figure 12 shows that as the proportion of rice husk increases, the degree of liquid phase polymerization improves, with the slag from the 20% rice husk addition sample exhibiting the highest polymerization degree.
As shown in Figure 13, Peak fitting was further performed on the Raman spectra to obtain the proportion of silicon-oxygen structures in the melt. Table 7 lists the characteristic structures involved in peak fitting and their center positions. Similarly, Qn(Si) (n=0~4) represents the silicate tetrahedra ([SiO4]), where n refers to the number of bridging oxygen atoms (BO) in the tetrahedron. A larger n indicates a higher degree of polymerization of the [SiO4] units[63]. This confirms that the addition of rice husk overall increases the polymerization degree of the silicon-oxygen structure in the slag, achieving physical encapsulation of heavy metal elements. It can thus be seen that when the rice husk addition is less than 15%, Cu and Cr elements are affected by both physical encapsulation and chemical immobilization, leading to decreased leaching concentrations. However, when the rice husk addition exceeds 15%, influenced by chemical immobilization factors, the leaching concentrations of Cu and Cr increase. For the Zn element, the leaching concentration continuously decreases with increasing rice husk proportion.
Combined with the previous thermodynamic equilibrium calculations and heavy metal content analysis, Figure 14 illustrates the mechanism diagram of heavy metal immobilization in gasification slag by rice husk addition. The core mechanism of heavy metal immobilizationis shown as follow. On one hand, the active SiO2 introduced by rice husk promotes the formation of low-melting eutectic phases (e.g., spinel, anorthite), improving slag fluidity and facilitating vitrification. It also significantly enhances the polymerization degree of silicate tetrahedra in the slag, forming highly polymerized silicate network structures (Q3, Q4), thereby strengthening the physical encapsulation capacity for heavy metals. On the other hand, it involves the mineral phase transformation of heavy metals. As the rice husk proportion increases, the proportion of the residual fraction (F4) for Cu, Zn and Cr rises significantly, indicating their transformation from extractable forms to stable forms. Cr3+ enters spinel, garnet lattices, or iron oxide phases via solid solution; Zn2+ is chemically immobilized by entering spinels or replacing Ca2+ in silicates to form Zn2SiO4; Cu forms Cu2O or silicate eutectic phases.
Leaching toxicity data further show that when adding 10%−15% rice husk, the leaching concentrations of Cr and Zn decrease from 41.60 and 108.00 mg/L to 5.89 and 7.10 mg/L, respectively, indicating that heavy metals are stably immobilized in mineral phases and are not easily extracted by acid.
In summary, the amount of rice husk addition exhibits a dual regulatory effect. An addition of 5%−10% promotes the formation of low-melting eutectic phases, enhances slag fluidity and the degree of vitrification, and strengthens the encapsulation and bonding capabilities for heavy metals. Conversely, an addition exceeding 15% leads to the dilution of alkaline oxides, which inhibits the expansion of the low-temperature melt. Furthermore, the introduced potassium elements promote the formation of gaseous double-salt chlorides such as KZnCl3/NaZnCl3, partially weakening the immobilization capacity within silicate minerals like melilite. Simultaneously, the increased FeO content may compete for Cu2+ adsorption sites, resulting in an increase of Cu leaching. Additionally, the volatilization of Cu and Zn intensifies at high temperatures (>1400 °C), and their Residual Rates (RR) decrease with increasing temperature. Therefore, for practical solid waste resource utilization, the optimal process conditions are identified as 1300−1400 °C, balancing slag fluidity, heavy metal residual rate, and energy consumption, combined with a 5%−10% rice husk addition. This approach enables the comprehensive optimization of the slag towards high polymerization, low leaching, and high residual rates. These findings provide a theoretical basis for the synergistic treatment of landfilled waste and biomass. The slag co-treated with rice husk possesses the potential for safe resource utilization in applications such as construction materials and road base layers.
3　Conclusions
Less
This study investigated the migration of heavy metals and the polymerization behavior of silicates in gasification slag from rice husk and landfilled municipal solid waste. In the gasification slag of landfilled waste, rice husk, as a silicon source, plays multiple roles in regulating melting behavior, strengthening silicate polymerized structures, and immobilizing heavy metals. The aim is to achieve efficient heavy metal immobilization, slag vitrification, and syngas recovery through the co-gasification technology of landfilled waste and rice husk, providing a feasible solution for the clean and efficient resource treatment of stockpiled waste. The conclusions obtained are as follows:
Adding rice husk (5%−10%) can reduce the flow temperature of the slag, reaching a minimum of 1213 °C. This is mainly attributed to the active SiO2 introduced by rice husk reacting with CaO and Fe2O3 in the waste ash to form low-melting eutectic phases such as anorthite, promoting the formation of low-temperature melts.
As the proportion of rice husk addition increases, the leaching concentrations of Cr, Zn and Cu in the slag significantly decrease. When adding 10%−15% rice husk, the leaching concentrations of Cr and Zn decrease from 41.60 and 108.00 mg/L to 5.89 and 7.10 mg/L, respectively. The amorphous SiO2 provided by rice husk increases the polymerization degree of silicate tetrahedra in the slag, promotes the formation of highly polymerized silicate networks, enhances the physical encapsulation and structural immobilization capacity for heavy metals, and reduces non-bridging oxygen sites, thereby inhibiting heavy metal leaching.
The volatilization of Cu and Zn is enhanced at high temperatures (>1400 °C), with their residual rates decreasing to 33%−60% and 31%−55%, respectively, as temperature rises. In contrast, Cr, due to its high boiling point and stable chemical properties, maintains a residual rate of 70%−123%. Rice husk promotes the transformation of heavy metals from acid-soluble and reducible fractions to the residual fraction, enhancing their environmental stability. The SiO2 introduced by rice husk promotes the formation of stable mineral phases for heavy metals, locking them within the crystal lattice and reducing their bioavailability and leaching risk.
References
Less
1
LI Q, MAO M, HUANG X, et al. Refined resource treatment of stale domestic garbage: Technological progress and value research[J]. J Publ Mgmt, 2022, 19(2): 142−153+175.
2
CHEN L. Physical and chemical properties and bacterial diversity of different landfill age refuse[D]. Qingdao: Qingdao University of Technology, 2018.
3
VONGDALA N, TRAN H, XUAN T, et al. Heavy metal accumulation in water, soil, and plants of municipal solid waste landfill in Vientiane, Laos[J]. Int J Env Res Pub He, 2019, 16(1): 22.
4
RAHOTHAN U, KHEMKHAO M, KAEWPENGKROW P. Solid waste management by RDF production from landfilled waste to renewable fuel of Nonthaburi[J]. Int J Renew Energy D, 2023, 12(5): 968.
5
ZHENG J. Study on carbon content per unit calorific value of coals in China[J]. Coal Process Compr Util, 2022, 1: 58−62.
6
SANTOS S, NOBRE C, BRITO P, et al. Brief overview of refuse-derived fuel production and energetic valorization: applied technology and main challenges[J]. Sustainability-Basel, 2023, 15(13): 10342.
7
PEDRAZZI S, SANTUNIONE G, MINARELLI A, et al. Energy and biochar co-production from municipal green waste gasification: A model applied to a landfill in the north of Italy[J]. Energ Convers Manage, 2019, 187: 274−282.
8
SUN Q, SUN B, WANG D, et al. A review on the chemical speciation and influencing factors of heavy metals in Municipal Solid Waste landfill humus[J]. WDSE, 2024, 6(2): 209−218.
9
KE C, MA X, TANG Y, et al. Effects of natural and modified calcium-based sorbents on heavy metals of food waste under oxy-fuel combustion[J]. Bioresour Technol, 2019, 271: 251−257.
10
OYEDELE D, GASU M, AWOTOYE O. Changes in soil properties and plant uptake of heavy metals on selected municipal solid waste dump sites in Ile-Ife, Nigeria[J]. Afr J Environ Sci Technol, 2008, 2(5): 107−115.
11
WILLNER J, FORNALCZYK A, JABLONSKA-CZAPLA M, et al. Studies on the content of selected technology critical elements (germanium, tellurium and thallium) in electronic waste[J]. Materials, 2021, 14(13): 3722.
12
SHIMOKURI D, FUKUBA S, ISHIZUKA S. Fundamental investigation on the fuel-NOx emission of the oxy-fuel combustion with a tubular flame burner[J]. P Combust Inst, 2015, 35(3): 3573−3580.
13
OKADA T, TOMIKAWA H. Effects of chemical composition of fly ash on efficiency of metal separation in ash-melting of municipal solid waste[J]. Waste Manage, 2013, 33(3): 605−614.
14
YOO H, LEE S, CHO S, et al. Evaluation of the melting gasification process for recovery of energy and resources from automobile shredder residues[J]. Energies, 2022, 15(3): 1248.
15
XIA M, ZHAO Y, ZHANG R, et al. Study on phase structure of molten slag from high- calcium MSWI fly ash vitrification[J]. Nonferrous Met Eng Res, 2018, 39(4): 85−90.
16
LI R, NIE Y, WANG L, et al. Migration characteristics experiment of heavy metal in the vitrification course of fly ash from municipal solid waste incineration[J]. Chin Environ Sci, 2004, 24(4): 480−483.
17
JIANG X, DUAN Y, LV G, et al. Research progress on the mechanism and systematic evaluation methods of solidification and stabilization of heavy metals in municipal solid waste incineration fly ash[J]. Chin J Environ Eng, 2022, 16(1): 10−19.
18
CLARKE L, SLOSS L. Trace elements emissions from coal combustion and gasification.[J]. IEA Coal Res Rep, 1992, 49: 13−14.
19
LI B, ZHANG W, JIA F, et al. Research on the combustion performance of municipal solid waste in different sorting scenarios: thermokinetics investigation via TG–DSC–FT-IR–MS[J]. ACS Omega, 2023, 9(1): 1206−1215.
20
WANG S. Volatilization Characteristics of typical heavy metals during the co-combustion of municipal solid waste and aged refuse[D].Guangzhou: South China University of Technology, 2023.
21
RANADEV P, NAGARAJU K, KUMARI R V, et al. Evaluating the stability of post mushroom substrate (PMS) and other agro-wastes for mass production of entomopathogenic fungi[J]. Curr J Appl Sci Technol, 2023, 42(13): 1−9.
22
WANG X, ZHANG J, CHEN Z, et al. Utilization of domestic waste biomass char in the context of carbon neutrality—low NOx decoupled combustion[J]. J Fuel Chem Technol, 2023, 51(8): 1165−1172.
23
HOSSAIN N, NIZAMUDDIN S, SHAH K. Thermal-chemical modified rice husk-based porous adsorbents for Cu (II), Pb (II), Zn (II), Mn (II) and Fe (III) adsorption[J]. J Water Process Eng, 2022, 46: 102620.
24
AHIDUZZAMAN M D, SADRUL ISLAM A K M. Preparation of porous bio-char and activated carbon from rice husk by leaching ash and chemical activation[J]. Springerplus, 2016, 5(1): 1248.
25
SHI Y, DAN R, YUAN H. Adsorption effect and mechanism of modified rice husk biochar on methyl orange in aqueous solution[J]. Environ. Sci, 2019, 40(6): 2783−2792.
26
LATA S, SAMADDER S R. Removal of heavy metals using rice husk: a review[J]. Int J Environ Res Dev, 2014, 4(2): 165−170.
27
LIANG A. Study on co-combustion characteristics of textile dyeing sludge-rice husk/ramie and stabilization mechanism of heavy metals[D]. Wuhan: Wuhan University, 2019.
28
FENG C, TANG J, GAO L, et al. Effects of CaO/SiO2 on viscous behaviors and structure of CaO-SiO2-11.00% MgO-11.00% Al2O3-43.00% TiO2 slag systems[J]. ISIJ Int, 2019, 59(1): 31−38.
29
LIAO W, ZHANG X, YANG R, et al. Biochar structure regulation based on the evaluation of adsorption efficiency, anti-aging ability and economy during soil heavy metal remediation[J]. J Anal Appl Pyrolysis, 2025: 107223.
30
MA X, LI F, MA M, et al. Fusion characteristics of blended ash from Changzhi coal and biomass[J]. J Fuel Chem Technol, 2018, 46(2): 129−137.
31
YANG G, REN Q, LI P, et al. Co-melting characteristics of MSWI fly ash and rice husk ash[J]. Combust Sci Technol, 2022, 28(5): 617−624.
32
LEBENDIG F, MÜLLER M. Influence of biofuel blending on inorganic constituent behavior and impact in Fluidized-bed gasification[J]. Energy Fuels, 2025, 39(8): 3868−3881.
33
PUTRA H, DEWI K, DAMANHURI E, et al. Conversion of organic fraction of municipal solid waste into solid fuel via hydrothermal carbonization[J]. Int J Eng Technol, 2018, 7(4): 4030−4034.
34
FAISAL M, MUNDU M, NNAMCHI S. Evaluation of the heating (Calorific) value of municipal wet solid waste from Kabagarame Dumping site in Bushenyi District, Uganda[J]. IDOSR Jsr, 2023, 8: 148−160.
35
JIA G. Combustion characteristics and kinetic analysis of biomass pellet fuel using thermogravimetric analysis[J]. Processes, 2021, 9(5): 868.
36
LEES H, JÄRVIK O, KONIST A, et al. Comparison of the ecotoxic properties of oil shale industry by-products to those of coal ash[J]. Oil Shale, 2022, 39(1): 1−19.
37
NETO O. Impacts of a large-scale model of municipal solid waste: An Input-Output analysis for the largest brazilian metropolitan region[J]. Heliyon, 2021, 7(5).
38
GERASSIMIDOU S, VELIS C, WILLIAMS P, et al. Chlorine in waste-derived solid recovered fuel (SRF), co-combusted in cement kilns: A systematic review of sources, reactions, fate and implications[J]. Crit Rev Env Sci Tec, 2021, 51(2): 140−186.
39
BEI J, XIANG W, LIN X, et al. Study on dioxins formation characteristics and TUA inhibitors in reducing atmosphere at low temperature[J]. Acta Sci Circumstantiae, 2023, 43(11): 282−289.
40
LI R, NIE Y, LI A. Study on physical chemical characteristics of fly ash from municipal solid waste incinerator[J]. J Fuel Chem Technol, 2004, 32(2): 175−179.
41
HONG X, LIU X, TANG L. Progress in physicochemical properties of ash/slag from co-gasification of agroforestry waste biomass and coal[J]. J Fuel Chem Technol, 2022, 50(6): 641−651.
42
SIMONOV A, MISHENKO T, YAZYKOV N, et al. Combustion and processing of rice husk in the vibrofluidized bed of catalyst or inert material[J]. Chem Sustainable Dev, 2003, 1: 277−284.
43
ZHANG J, DIAO H, WANG M, et al. Effects of rice husk and sewage sludge co-pyrolysis on characteristics of the sludge biochar and its ecological risk of heavy metals[J]. Acta Sci Circumstantiae, 2019, 39: 1250−1256.
44
LI P, KAN H, CHEN C, et al. Melting and flow behavior of coal ash at high temperatures based on SiO2–Al2O3–CaO/Na2O pseudoternary phase diagram[J]. ACS Omega, 2024, 9(20): 22313−22324.
45
WEI Q, SONG W. Mineralogical and chemical characteristics of coal ashes from two high-sulfur coal-fired power plants in Wuhai, Inner Mongolia, China[J]. Minerals, 2020, 10(4): 323.
46
KONG X, DONG Y, ZHANG M, et al. Treatment technologies of fly ash from municipal solid waste incineration[J]. Chem Ind Eng Prog, 2024, 43(7): 4102.
47
ALTIKULAÇ A, TURHAN S, KURNAZ A, et al. Assessment of the enrichment of heavy metals in coal and its combustion residues[J]. ACS Omega, 2022, 7(24): 21239−21245.
48
LI Y, YANG D, ZHOU X, et al. Heavy metal migration characteristics of co-combustion between sewage sludge and high alkaline coal on circulating fluidized bed[J]. J Therm Sci, 2022, 31(6): 2178−2188.
49
LI S, VELA I C, JÄRVINEN M, et al. Polyethylene terephthalate (PET) recycling via steam gasification–The effect of operating conditions on gas and tar composition[J]. Waste Manage, 2021, 130: 117−126.
50
LU G, LIU H, HU H, et al. Fate of heavy metals in CaO-conditioned sludge gasification[J]. Chem Eng J, 2017, 68(1): 272−280.
51
MAMMARELLA D, DI GIULIANO A, GALLUCCI K. Reuse and valorization of solid digestate ashes from biogas production[J]. Energies, 2024, 17(3): 751.
52
WANG Y, NI W, ZHANG S, et al. Optimal mixture designs for heavy metal encapsulation in municipal solid waste incineration fly ash[J]. Appl Sci, 2020, 10(19): 6948.
53
LIU M, DUAN Y, BIKANE K, et al. The migration and transformation of heavy metals in sewage sludge during hydrothermal carbonization combined with combustion[J]. Biomed Res Int, 2018, 2018(1): 1913848.
54
ZHU G, WANG X, YIN X, et al. Influence of inherent minerals on metalworking fluids sludge pyrolysis: Products characterization and heavy metals behavior[J]. Heliyon, 2024, 10(4): e26256.
55
SUNGUR A, SOYLAK M, OZCAN H. Investigation of heavy metal mobility and availability by the BCR sequential extraction procedure: Relationship between soil properties and heavy metals availability[J]. Chem Spec Bioavailab, 2014, 26(4): 219−230.
56
ŁUKOWSKI A. Fractions of zinc, chromium and cobalt in municipal solid waste incineration bottom ash[J]. J Ecol Eng, 2022, 23(3): 12−16.
57
ZHANG F, LI Y, ZHANG J, et al. Effects of slag-based cementitious material on the mechanical behavior and heavy metal immobilization of mine tailings based cemented paste backfill[J]. Heliyon, 2022, 8(9): e10695.
58
CHU S, WU D, LIANG L, et al. Municipal sewage sludge compost promotes Mangifera persiciforma tree growth with no risk of heavy metal contamination of soil[J]. Sci Rep, 2017, 7(1): 1−11.
59
JIANG C, LI K, BI Z, et al. Developments in atomistic and nano structure evolution mechanisms of molten slag using atomistic simulation methods[J]. Nanomaterials-Basel, 2024, 14(5): 464.
60
BHATIA L, SAHU D. SEM & FT-IR analysis of rice husk to assess the impact of physiochemical pretreatment[J]. J Agric Ecol Res Int, 2023, 24(6): 1−13.
61
DAKHANE A, MADAVARAPU S, MARZKE R, et al. Time, temperature, and cationic dependence of alkali activation of slag: Insights from fourier transform infrared spectroscopy and spectral deconvolution[J]. Appl Spectrosc, 2017, 71(8): 1795−1807.
62
YUAN Z, CAI G, GAO L, et al. The physical encapsulation and chemical fixation of Zn during thermal treatment process of municipal solid waste incineration (MSWI) fly ash[J]. Waste Manage, 2023, 166: 203−210.
63
GAO J, WEN G, HUANG T, et al. Raman Spectroscopic study of the structure of CaO-SiO2-Al2O3-based flux[J]. Spectrosc Spectral Anal, 2016, 36(10): 3190−3196.
64
CHENG J S, XIAO Z, YANG K, et al. Viscosity, fragility and structure of Na2O–CaO–Al2O3–SiO2 glasses of increasing Al/Si ratio[J]. Ceram Int, 2013, (4): 4055−4062.
Appendix
Less
Year 2026 volume 54 Issue 7
PDF
149
64
Cite this Article
BibTeX
Article Info
doi: 10.1016/S1872-5813(26)60676-7
  • Receive Date：2025-10-14
  • Online Date：2026-09-23
  • Published：2026-07-10
Article Data
Affiliations
History
  • Received：2025-10-14
  • Revised：2025-11-27
  • Accepted：2026-01-07
Affiliations
    Institute of Clean Coal Technology, East China University of Science and Technology, Shanghai 200237, China

Corresponding:

References
Share
https://castjournals.cast.org.cn/joweb/rlhxxb/EN/10.1016/S1872-5813(26)60676-7
Share to
QR

Scan QR to access full text

Cite this article
BibTeX
Citations
表12种不同金属材料的力学参数
科
Family		 属数
Number of
genus		 种数
Number of
species		 占总种数比例
Percentage of
total species (%)		 属
Genus		 种数
Number of
species		 占总种数比例
Percentage of total
species (%)
鹅膏菌科Amanitaceae 2 11 5.26 鹅膏菌属 Amanita 10 4.78
小菇科 Mycenaceae 2 12 5.74 丝盖伞属 Inocybe 5 2.39
多孔菌科 Polyporaceae 8 14 6.70 蜡蘑属 Laccaria 5 2.39
红菇科 Russulaceae 3 23 11.00 小皮伞属 Marasmius 6 2.87
小菇属 Mycena 11 5.26
光柄菇属 Pluteus 5 2.39
红菇属 Russula 17 8.13
栓菌属 Trametes 5 2.39
关闭全屏
  • BibTeX
  • EndNote
  • RefWorks
  • TxT
Links
Articles
Latest Articles
Most Read
Collections
Updates
Events
News
Multimedia
About
About Us
Contact
No. 86 Xueyuan South Road, Haidian District, Beijing
100081
010-62662699(Operation and Technical Support)
qkjq@cast.org.cn

Copyright © 2025 China Association for Science and Technology. All rights reserved. For all open access content, the relevant licensing terms apply.
Sponsored by the Office of the Leading Group for Cybersecurity and Informatization of CAST, and supported by Science and Technology Review Publishing House