Numerical simulation of silica particle trajectory in flow field and silica particle spheroidizing in oxygen–acetylene flame spheroidization process

• Published in: Powder technology Vol. 286; pp. 451 - 458
• Main Authors: Ji, Zhengjia, Jin, Hongyun, Wu, Yaoqing, Li, Yunlong, Liu, Min, Xu, Chunhui, Hou, Pan, Dong, Jie, Hou, Shuen
• Format: Journal Article
• Language: English
• Published: Elsevier B.V 01.12.2015
• Subjects: CFD simulation; Oxygen–acetylene flame spheroidization process; Particle trajectory; Spherical silica; CFD simulation; Oxygen–acetylene flame spheroidization process; Particle trajectory; Spherical silica
• ISSN: 0032-5910; 1873-328X
• DOI: 10.1016/j.powtec.2015.07.040

A numerical simulation was developed for particle trajectory in flow field and spheroidizing of silica particle in oxygen–acetylene flame spheroidization process. Gas flow field and silica particle behavior in oxygen–acetylene flame spheroidization process was simulated using a Computational Fluid Dynamics (CFD) package FLUENT. A model was proposed for optimizing spheroidization process of silica particle. Oxygen gas and acetylene gas were used as the continuous phase. Silica particle was used as the dispersed phase. The three-dimensional, steady and isothermal flow field was showed for illustrating the continuous phase and the dispersed phase. Conservation equations of mass and momentum for each phase were solved using the finite volume numerical technique. Various gas conditions were discussed systematically. The injected silica particle trajectories were simulated by using dispersed particle surface trajectory. The trajectories and spheroidizations of different size particles were analyzed. The results of numerical simulation reveal that the flame length was reasonable and overall temperature was highest when acetylene gas flow rate was 10L·min−1, oxygen gas flow rate was 20L·min−1 and powder carrying gas flow rate was 5L·min−1 and 40μm silica particles were difficult to finish spheroidizing within 5×10−4s. The comparison shows that temperature distribution, velocity distribution, particle trajectories, and deformation which were predicted by simulation, were in good agreement with the corresponding experimental results. [Display omitted] •The gas flow field in furnace of oxygen–acetylene flame spheroidization process was modeled.•The trajectories of injected silica powder particles were calculated.•The spheroidization process of different size particles were simulated.•After passing through the flow field, spheroidization effects were predicted.