Liquid-Phase-Assisted Catalytic Nitridation of Silicon and In Situ Growth of α-Si3N4

Si3N4 powders were synthesized with Fe, Co, or Ni as catalysts using Si powder at 1250 °C in a nitrogen atmosphere by liquid-phase-assisted catalytic nitridation synthesis (LPA–CNS). The catalytic effects of the metals on the nitridation of silicon powder were investigated by mixing the powder with 2 wt% by mass of Fe, Co, or Ni in a high-temperature liquid phase in flowing nitrogen. The α-Si3N4 micro-morphology could be effectively changed by adjusting the type of catalyst in the initial reaction mixtures. Fe, Co, and Ni promoted the formation of α-Si3N4 at 1250 °C and controlled the morphology of the α-Si3N4 particles. The hexagonal flakes of α-Si3N4 with a better defined morphology were obtained using Ni as the catalyst, compared to that obtained from the other two catalysts.


Introduction
Si 3 N 4 -based ceramics have been widely used in steel, aerospace, chemical, and electronic fields due to their strong oxidation resistance, stable chemical properties, and excellent mechanical properties [1][2][3][4][5]. In general, α-Si 3 N 4 powder is preferred to β-Si 3 N 4 powder as a raw material for fabricating compacted bodies because the α-Si 3 N 4 starting powder has a higher reactivity that easily forms elongated Si 3 N 4 grain morphology, which has excellent mechanical properties [4,5]. Due to these appealing properties, Si 3 N 4 has been widely studied and has become the most promising structural material, especially for high temperature applications [6,7]. However, the high cost of fine Si 3 N 4 powders is the prime obstacle to the regular application of Si 3 N 4 -based materials. Therefore, the fabrication of α-Si 3 N 4 powders with tailored properties through a cost-effective synthesis method is a research topic of great interest.
At present, the preparation methods of silicon nitride are mainly divided into organic preparation methods and inorganic preparation methods. The organic method is mainly used to synthesize precursors and to prepare silicon nitride through the pyrolysis of the precursors [8][9][10]. Some inorganic preparation methods have been adopted to prepare silicon nitride powder, including the nitridation of Si powder [11], carbothermal reduction nitridation [12,13], and combustion synthesis [14,15]. However, these techniques still suffer various disadvantages, such as a broad particle size distribution, difficulty in size and composition control, powder reunion, high nitridation temperature, and long holding time. High temperature liquid phase synthesis method is an environmentally friendly technology, widely applied in the preparation of powder [16][17][18][19], nano coating [20][21][22][23], and porous materials [24][25][26]. However, there are only a few available reports on the high temperature liquid phase synthesis of silicon nitride powder.
It was well known that transition elements can regulate the kinetics of Si nitridation and accelerate the growth of α-Si 3 N 4 [27,28]. It should be noted that, although it has been reported that metals, metal oxides, metal nitrates, or metal nanoparticles were used Materials 2022, 15, 6074 2 of 9 as a catalyst for the accelerated nitridation of Si powder [29][30][31][32][33][34], most of the previous studies have focused on the limited choices of catalysts and complex synthesis methods. In addition, the enhancement of α-Si 3 N 4 formation is strictly limited to the presence of molten alloy liquid phases [34,35] but most catalysts do not play a distinctly accelerated role in the information of α-Si 3 N 4 powder. Other research groups have made some attempts on controllable preparation of α-Si 3 N 4 [36,37] including our previous contribution [38][39][40]. However, the influence of different transition metal catalysts on the fabrication of α-Si 3 N 4 powder is still unclear.
In this study, the synthesis of Si 3 N 4 powder with different microstructures from by liquid-phase-assisted catalytic nitridation synthesis (LPA-CNS) in the NaCl-NaF molten salt system. The nitridation processes were carried out simultaneously with the three metal catalysts under identical reaction conditions, such as nitridation temperature, nitridation time and catalyst amount.

Materials and Methods
The details of the synthesis process are described as follows: 35 wt% Si powder (99% purity, grain size 9 µm, Beijing Xing Rong Yuan Technology Co. Ltd., Beijing, China); 65 wt% analytical grade salt mixture composed of 95 wt% sodium chloride (NaCl, 99% purity, Sinopharm Chemical Reagent Co., Ltd., Shanghai, China) and 5 wt% sodium fluoride (NaF, 99% purity, Sinopharm Chemical Reagent Co., Ltd., Shanghai, China); and 2 wt% Fe, Co, or Ni powder (99.99% purity, grain size 2 µm, Beijing Xing Rong Yuan Technology Co., Ltd., Beijing, China) were dry-mixed in an alumina mortar for 1 h. Then, five grams of the mixed powder containing Si and Na salts and the catalyst were placed in an alumina crucible. The nitridation of the silicon powder was carried out in a vertical alumina tube furnace, which is shown as a diagram in Figure 1 together with the gas supply system and vacuum system. Since the reaction between N 2 and Si is highly exothermic, the samples were initially heated at 1150 • C for 1 h in the alumina-tube furnace. The reaction temperature was then raised to 1250 • C and the reaction was continued for 5 h under a nitrogen atmosphere. After cooling to 25 • C under nitrogen, the as-obtained solidified mass was repeatedly washed with hot distilled water and filtered to remove the residual salts. Finally, the obtained silicon nitride paste, prior to its characterization, was dried in oven at 110 • C for 12 h. It was well known that transition elements can regulate the kinetics of Si nitridation and accelerate the growth of α-Si3N4 [27,28]. It should be noted that, although it has been reported that metals, metal oxides, metal nitrates, or metal nanoparticles were used as a catalyst for the accelerated nitridation of Si powder [29][30][31][32][33][34], most of the previous studies have focused on the limited choices of catalysts and complex synthesis methods. In addition, the enhancement of α-Si3N4 formation is strictly limited to the presence of molten alloy liquid phases [34,35] but most catalysts do not play a distinctly accelerated role in the information of α-Si3N4 powder. Other research groups have made some attempts on controllable preparation of α-Si3N4 [36,37] including our previous contribution [38][39][40]. However, the influence of different transition metal catalysts on the fabrication of α-Si3N4 powder is still unclear.
In this study, the synthesis of Si3N4 powder with different microstructures from by liquid-phase-assisted catalytic nitridation synthesis (LPA-CNS) in the NaCl-NaF molten salt system. The nitridation processes were carried out simultaneously with the three metal catalysts under identical reaction conditions, such as nitridation temperature, nitridation time and catalyst amount.

Materials and Methods
The details of the synthesis process are described as follows: 35 wt% Si powder (99% purity, grain size 9 μm, Beijing Xing Rong Yuan Technology Co. Ltd., Beijing, China); 65 wt% analytical grade salt mixture composed of 95 wt% sodium chloride (NaCl, 99% purity, Sinopharm Chemical Reagent Co., Ltd., Shanghai, China) and 5 wt% sodium fluoride (NaF, 99% purity, Sinopharm Chemical Reagent Co., Ltd., Shanghai, China); and 2 wt% Fe, Co, or Ni powder (99.99% purity, grain size 2 μm, Beijing Xing Rong Yuan Technology Co., Ltd., Beijing, China) were dry-mixed in an alumina mortar for 1 h. Then, five grams of the mixed powder containing Si and Na salts and the catalyst were placed in an alumina crucible. The nitridation of the silicon powder was carried out in a vertical alumina tube furnace, which is shown as a diagram in Figure 1 together with the gas supply system and vacuum system. Since the reaction between N2 and Si is highly exothermic, the samples were initially heated at 1150 °C for 1 h in the alumina-tube furnace. The reaction temperature was then raised to 1250 °C and the reaction was continued for 5 h under a nitrogen atmosphere. After cooling to 25 °C under nitrogen, the as-obtained solidified mass was repeatedly washed with hot distilled water and filtered to remove the residual salts. Finally, the obtained silicon nitride paste, prior to its characterization, was dried in oven at 110 °C for 12 h.  The product was collected, and samples were prepared accordingly for various characterization techniques. The phase composition of the as-prepared samples was identified by X-ray diffraction (XRD, X'Pert Pro, Philips, Eindhoven, The Netherlands) analysis. The spectra from 10 • to 80 • (2θ) were recorded using Cu Kα radiation (λ = 0.154 nm) at 40 mA and 40 kV, at a scan rate of 2 • /min and a step size of 0.03 • . ICSD cards No. 035561, 074749 and 043403 were cited, respectively. The infrared (IR) spectra of the samples were recorded on a Fourier transform infrared (FTIR, NICOLET iS50, Thermo Fisher Scientific, Waltham, MA, USA) spectrometer in the range 300-4000 cm −1 . The microstructure of the samples was characterized using a field-emission scanning electron microscope (FESEM, Nova nano 400, FEI, Waltham, MA, USA) and a transmission electron microscope (TEM, JEM2100, JEOL, Tokyo, Japan). Samples for SEM analysis were coated with gold. Samples for TEM analysis were dispersed in absolute ethanol by ultrasonication, and a drop of the suspension was placed on a copper grid and air-dried. Selected-area electron diffraction (SAED) along with energy dispersive spectroscopy (EDS) was used to identify the phase composition of the samples. Finally, the property of powder was characterized by Brunauer-Emmett-Teller (BET, Autosorb-1-MP/LP, Quantachrome, Boynton Beach, FL, USA).

Results
A series of experiments were performed in which the type of catalyst was varied. There are amounts of unreacted Si and a small amount of α-Si 3 N 4 in the catalyst-free sample, which indicates that only a small amount of Si has been nitrided, as shown in Figure 2a. However, it can be clearly seen that the residual Si peaks (corresponding to (111), (220), (311) and (331)) distinctly decreased or disappeared. Meanwhile, both α-Si 3 N 4 and β-Si 3 N 4 were identified in the samples containing catalyst, indicating that Si powder should be nitrided completely under the effects of Fe, Co, and Ni catalysts. Moreover, Ni catalysts give a higher intensity of α-Si 3 N 4 phase when compared with using Co and Fe, indicating that the amount of α-Si 3 N 4 in the samples containing Ni is more than those in samples containing Co or Fe. The relative contents of crystalline phases in the samples with various catalysts after 5 h nitridation at 1250 • C were calculated by the Rietveld refinement method, and the results are shown in Figure 2b. The addition of transition metal catalyst in Si powder led to a higher content of α-Si 3 N 4 phase than that obtained from the catalyst-free sample. Only 52.4 wt% α-Si 3 N 4 was formed in the catalyst-free samples. On the contrary, the samples containing the Fe, Co, and Ni catalysts demonstrated over 95.6% α-Si 3 N 4 and less than 4.4% β-Si 3 N 4 in the final product. Therefore, adding these transition metals into silicon raw material is a promising choice for the quality improvement of the α-Si 3 N 4 produced by the high temperature liquid phase synthesis method.  The as-prepared α-Si3N4 samples were further characterized by FTIR. The FTIR spectra of the sample in Figure 3 show two absorption bands, one at 800-1100 cm −1 with a peak maximum at ~942 cm −1 and the other at 400-600 cm −1 with a peak maximum at ~493 cm −1 , which correspond to the Si-N-Si asymmetric and symmetric stretching modes, respectively [41]. The bands at 942, 890, 853, 680, 594, 493, 457, and 405 cm −1 indicate the distinct absorptions of α-Si3N4 [42]. These bands become sharper in the spectra of the samples with the added catalysts, indicating the formation of a well-defined crystal structure of the α-Si3N4 phase. The peak at 1183 cm −1 corresponds to the stretching vibration of Si-Si bonds owing to unreacted silicon in the catalyst-free sample [43]. The peak at 1637 cm −1 is attributed to the water absorbed during the analysis [44]. The superimposed IR spectrum of The as-prepared α-Si 3 N 4 samples were further characterized by FTIR. The FTIR spectra of the sample in Figure 3 show two absorption bands, one at 800-1100 cm −1 with a peak maximum at~942 cm −1 and the other at 400-600 cm −1 with a peak maximum at 493 cm −1 , which correspond to the Si-N-Si asymmetric and symmetric stretching modes, respectively [41]. The bands at 942, 890, 853, 680, 594, 493, 457, and 405 cm −1 indicate the distinct absorptions of α-Si 3 N 4 [42]. These bands become sharper in the spectra of the samples with the added catalysts, indicating the formation of a well-defined crystal structure of the α-Si 3 N 4 phase. The peak at 1183 cm −1 corresponds to the stretching vibration of Si-Si bonds owing to unreacted silicon in the catalyst-free sample [43]. The peak at 1637 cm −1 is attributed to the water absorbed during the analysis [44]. The superimposed IR spectrum of α-Si 3 N 4 further confirms the formation of α-Si 3 N 4 as the primary phase in the samples, corroborating with the XRD results. In addition, it confirms the presence of residual Si in the catalyst-free sample, as shown in Figure 3.
which correspond to the Si-N-Si asymmetric and symmetric stretching modes, tively [41]. The bands at 942, 890, 853, 680, 594, 493, 457, and 405 cm −1 indicate the absorptions of α-Si3N4 [42]. These bands become sharper in the spectra of the samp the added catalysts, indicating the formation of a well-defined crystal structure o Si3N4 phase. The peak at 1183 cm −1 corresponds to the stretching vibration of Si-S owing to unreacted silicon in the catalyst-free sample [43]. The peak at 1637 cm tributed to the water absorbed during the analysis [44]. The superimposed IR spec α-Si3N4 further confirms the formation of α-Si3N4 as the primary phase in the s corroborating with the XRD results. In addition, it confirms the presence of resid the catalyst-free sample, as shown in Figure 3. The detailed microstructure and elemental composition of the as-prepared Si ples were examined by FESEM and EDS analysis (insets in Figure 4 and Table  images of the samples containing 2 wt% Fe, Co, and Ni are shown in Figure 4. T dation product mainly consists of irregularly elongated particles, equiaxed flak short rod-like and hexagonal plate-like grains. As shown in Figure 4a, the cata sample contains many equiaxial grains with diameters in the micron range, and t merous grains aggregate to form large particles. Spectra obtained from EDS a given as the inset in Figure 4a, confirm the presence of only N and Si in the granu ticles. As seen in Figure 4b, a number of anomalous elongated grains are observe samples obtained using the Fe catalyst. Coarse granular agglomerates, compos Si3N4 particles, are randomly distributed in the samples, as shown in Figure 4b. T image in Figure 4c reveals that coarse equiaxial flakes and glossy rod-like grai agglomerates on the surface of the sample obtained using Co powder as the catal ilar to our previous results [38]. On the other hand, the SEM image of the sample o using the Ni catalyst (Figure 4d) indicates the formation of well-developed he plate-like α-Si3N4 grains with the thicknesses of several dozen nanometers, an grains are randomly distributed in the sample. EDS results (insets in Figure 4b  The detailed microstructure and elemental composition of the as-prepared Si 3 N 4 samples were examined by FESEM and EDS analysis (insets in Figure 4 and Table 1). SEM images of the samples containing 2 wt% Fe, Co, and Ni are shown in Figure 4. The nitridation product mainly consists of irregularly elongated particles, equiaxed flakes, and short rod-like and hexagonal plate-like grains. As shown in Figure 4a, the catalyst-free sample contains many equiaxial grains with diameters in the micron range, and then numerous grains aggregate to form large particles. Spectra obtained from EDS analysis, given as the inset in Figure 4a, confirm the presence of only N and Si in the granular particles. As seen in Figure 4b, a number of anomalous elongated grains are observed for the samples obtained using the Fe catalyst. Coarse granular agglomerates, composed of α-Si 3 N 4 particles, are randomly distributed in the samples, as shown in Figure 4b. The SEM image in Figure 4c reveals that coarse equiaxial flakes and glossy rod-like grains form agglomerates on the surface of the sample obtained using Co powder as the catalyst, similar to our previous results [38]. On the other hand, the SEM image of the sample obtained using the Ni catalyst (Figure 4d) indicates the formation of well-developed hexagonal plate-like α-Si 3 N 4 grains with the thicknesses of several dozen nanometers, and these grains are randomly distributed in the sample. EDS results (insets in Figure 4b-d and Table 1) show that the anomalous elongated grains, flake-like and rod-like particles, and hexagonal plates consist of Si and N; the elemental amounts correspond to the Si 3 N 4 phase, in agreement with the XRD and IR results.   TEM observations along with SAED analysis were further carried out to identify the crystalline structure of the Si3N4 samples generated at 1250 °C. Figure 5 shows the transmission electron microscopy and SAED images of the samples obtained with Fe, Co, and Ni as catalysts. The TEM image of the sample obtained with Fe as the catalyst (Figure 5a) shows that elongated and granular grains agglomerate to form larger granules. The equiaxial α-Si3N4 flakes aggregate together to form large particles in the product obtained with Co as the catalyst (Figure 5b), as seen in the corresponding SEM image. The TEM image of the sample obtained with Ni as the catalyst (Figure 5c) shows hexagonal Si3N4 plates. The related SAED patterns (insets in Figure 5a-c) confirm that the anomalous elongated TEM observations along with SAED analysis were further carried out to identify the crystalline structure of the Si 3 N 4 samples generated at 1250 • C. Figure 5 shows the transmission electron microscopy and SAED images of the samples obtained with Fe, Co, and Ni as catalysts. The TEM image of the sample obtained with Fe as the catalyst (Figure 5a) shows that elongated and granular grains agglomerate to form larger granules. The equiaxial α-Si 3 N 4 flakes aggregate together to form large particles in the product obtained with Co as the catalyst (Figure 5b), as seen in the corresponding SEM image. The TEM image of the sample obtained with Ni as the catalyst (Figure 5c Figure 6a shows nitrogen adsorption-desorption isotherms of samples containing different catalysts heated at 1250 °C for 5 h in NaCl-NaF molten salt media. The nitrogen adsorption capacity of samples increased sharply, and the adsorption curve was biased towards the y axis at the low pressure area (P/P0 = 0.0-0.1), indicating that there were stable micropores in the samples. Moreover, the adsorption capacity increased slowly at P/P0 = 0.3-0.8 and increased significantly at P/P0 = 0.9-1.0. It can be confirmed that the adsorption-desorption isotherms of samples are typical type II, according to the IUPAC classification [45]. It is worth noting that the adsorption isotherms of samples, through the addition of catalysts, had a long lagged loop at a high relative pressure area, indicating that there were many mesopores in the samples. On the other hand, the adsorption capacity of sample with Fe catalyst was larger than that of the other two samples. However, the adsorption isotherm of catalyst-free sample has no hysteresis loop. Figure 6b shows the specific surface area of samples without catalyst or by addition of Fe, Co, and Ni powder as catalyst. As shown in Figure 6b, the specific surface area of the sample without catalyst was 4.1 m 2 /g. In contrast, the specific surface area of samples with Fe, Co, and Ni powder  Figure 6a shows nitrogen adsorption-desorption isotherms of samples containing different catalysts heated at 1250 • C for 5 h in NaCl-NaF molten salt media. The nitrogen adsorption capacity of samples increased sharply, and the adsorption curve was biased towards the y axis at the low pressure area (P/P 0 = 0.0-0.1), indicating that there were stable micropores in the samples. Moreover, the adsorption capacity increased slowly at P/P 0 = 0.3-0.8 and increased significantly at P/P 0 = 0.9-1.0. It can be confirmed that the adsorption-desorption isotherms of samples are typical type II, according to the IUPAC classification [45]. It is worth noting that the adsorption isotherms of samples, through the addition of catalysts, had a long lagged loop at a high relative pressure area, indicating that there were many mesopores in the samples. On the other hand, the adsorption capacity of sample with Fe catalyst was larger than that of the other two samples. However, the adsorption isotherm of catalyst-free sample has no hysteresis loop. Figure 6b shows the specific surface area of samples without catalyst or by addition of Fe, Co, and Ni powder as catalyst. As shown in Figure 6b, the specific surface area of the sample without catalyst was 4.1 m 2 /g. In contrast, the specific surface area of samples with Fe, Co, and Ni powder was obviously improved. When Fe powder is used as a catalyst, the specific surface area of the sample reaches 14.5 m 2 /g. During Si 3 N 4 synthesis in molten salt system, silicon powder is slightly soluble in the molten salt system under high temperature conditions, and the dissolved silicon exists in the form of atoms or atomic groups. As the temperature increases, the surface tension and viscosity of the molten salt decrease significantly, and the dissolution and diffusion of silicon powder in the molten salt intensifies [22,39]. The introduction of catalysts has a crucial effect on the composition and microstructure of Si 3 N 4 powder in the NaCl-NaF molten salt media. It was worth noting that the crystal shape of α-Si 3 N 4 could be converted to anomalously elongated, granular, or hexagonal plate-like form by the addition of Fe, Co, or Ni. When metal catalysts are present in the samples, the mechanism of Si powder nitridation in the samples is that M-Si (M = Fe, Co and Ni) liquid phase was formed by reactions between metal (Fe, Co or Ni) and Si at low temperature. Moreover, the nucleation and growth of Si 3 N 4 were controlled by different reactions in the molten salt media. Firstly, Si 3 N 4 nucleation was mainly controlled by gas-solid reaction between dissolved Si atom and N 2 . While the growth of Si 3 N 4 grain was established to be reaction between Si(g)/Si(l) and N/N 2 in the system. However, there began to appear liquid phase in the samples containing Fe, Co, and Ni catalysts at different temperature. Therefore, amount of Si(g)/Si(l) in the system varied with catalyst type at nitridation temperature, which also marked Si 3 N 4 crystal preferential growth in different directions. A mechanism for the catalytic of nitridation of Si powder is shown in Figure 7.  Figure 6a shows nitrogen adsorption-desorption isotherms of samples containing different catalysts heated at 1250 °C for 5 h in NaCl-NaF molten salt media. The nitrogen adsorption capacity of samples increased sharply, and the adsorption curve was biased towards the y axis at the low pressure area (P/P0 = 0.0-0.1), indicating that there were stable micropores in the samples. Moreover, the adsorption capacity increased slowly at P/P0 = 0.3-0.8 and increased significantly at P/P0 = 0.9-1.0. It can be confirmed that the adsorption-desorption isotherms of samples are typical type II, according to the IUPAC classification [45]. It is worth noting that the adsorption isotherms of samples, through the addition of catalysts, had a long lagged loop at a high relative pressure area, indicating that there were many mesopores in the samples. On the other hand, the adsorption capacity of sample with Fe catalyst was larger than that of the other two samples. However, the adsorption isotherm of catalyst-free sample has no hysteresis loop. Figure 6b shows the specific surface area of samples without catalyst or by addition of Fe, Co, and Ni powder as catalyst. As shown in Figure 6b, the specific surface area of the sample without catalyst was 4.1 m 2 /g. In contrast, the specific surface area of samples with Fe, Co, and Ni powder was obviously improved. When Fe powder is used as a catalyst, the specific surface area of the sample reaches 14.5 m 2 /g.  was obviously improved. When Fe powder is used as a catalyst, the specific surface area of the sample reaches 14.5 m 2 /g. During Si3N4 synthesis in molten salt system, silicon powder is slightly soluble in the molten salt system under high temperature conditions, and the dissolved silicon exists in the form of atoms or atomic groups. As the temperature increases, the surface tension and viscosity of the molten salt decrease significantly, and the dissolution and diffusion of silicon powder in the molten salt intensifies [22,39]. The introduction of catalysts has a crucial effect on the composition and microstructure of Si3N4 powder in the NaCl-NaF molten salt media. It was worth noting that the crystal shape of α-Si3N4 could be converted to anomalously elongated, granular, or hexagonal plate-like form by the addition of Fe, Co, or Ni. When metal catalysts are present in the samples, the mechanism of Si powder nitridation in the samples is that M-Si (M = Fe, Co and Ni) liquid phase was formed by reactions between metal (Fe, Co or Ni) and Si at low temperature. Moreover, the nucleation and growth of Si3N4 were controlled by different reactions in the molten salt media. Firstly, Si3N4 nucleation was mainly controlled by gas-solid reaction between dissolved Si atom and N2. While the growth of Si3N4 grain was established to be reaction between Si(g)/Si(l) and N/N2 in the system. However, there began to appear liquid phase in the samples containing Fe, Co, and Ni catalysts at different temperature. Therefore, amount of Si(g)/Si(l) in the system varied with catalyst type at nitridation temperature, which also marked Si3N4 crystal preferential growth in different directions. A mechanism for the catalytic of nitridation of Si powder is shown in Figure 7.

Conclusions
In summary, to meet the high-quality powder requirements for the preparation of ceramic substrates with low grain boundary size defects, a high α form Si 3 N 4 powder with multiple morphologies was obtained through the nitridation of Si in molten state via the reaction of Si powder mixed with Na salts under N 2 atmosphere in the presence of various transition metal catalysts. The nitridation of Si powder with 2 wt% catalysts (Fe, Co, or Ni) was carried out at 1250 • C for 5 h. While only 52.4 wt% α-Si 3 N 4 was present in the catalyst-free sample, there were about 96 wt% α-Si 3 N 4 and 4 wt% β-Si 3 N 4 in the samples obtained using 2 wt% Ni, Fe, and Co, under the same reaction conditions. The addition of Fe, Co, and Ni catalysts not only promoted the formation of α-Si 3 N 4 but also influenced the morphology of α-Si 3 N 4 particles. When using Fe as the catalyst, several anomalously elongated α-Si 3 N 4 grains were obtained, and randomly distributed in the sample. When using Co and Ni as the catalysts, equiaxial flake-like and rod-like α-Si 3 N 4 particles, and hexagonal plate-like α-Si 3 N 4 particles were obtained, respectively. The growth mechanism of α-Si 3 N 4 was confirmed, which was mainly a vapor-solid or vapor-liquid-solid pattern.