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Crystallization and viscosity-temperature characteristics during co-gasification of industrial sludge and coal

熔渣(焊接) 结晶 粘度 材料科学 粉煤灰 扫描电子显微镜 傅里叶变换红外光谱 化学工程 聚合 分析化学(期刊) 冶金 化学 复合材料 聚合物 色谱法 有机化学 工程类
作者
Linmin Zhang,Bin Liu,Juntao Wei,Xudong Song,Yonghui Bai,Jiaofei Wang,Ying Zhou,Huijun Yang,Guangsuo Yu
出处
期刊:Frontiers in energy [Springer Nature]
卷期号:16 (6): 1037-1047 被引量:4
标识
DOI:10.1007/s11708-022-0824-x
摘要

Co-gasification of industrial sludge (IS) and coal was an effective approach to achieve harmless and sustainable utilization of IS. The long-term and stable operation of a co-gasification largely depends on fluidity of coal-ash slag. Herein, the effects of IS addition on the crystallization and viscosity of Shuangmazao (SMZ) coal were investigated by means of high temperature stage coupled with an optical microscope (HTSOM), a scanning electron microscopy coupled with an energy dispersive X-ray spectrometry (SEM-EDS), X-ray diffraction (XRD), a Fourier transform infrared spectrometer (FTIR), and FactSage software. The results showed that when the proportion of IS was less than 60%, with the addition of IS, the slag existed in an amorphous form. This was due to the high content of SiO2 and Al2O3 in SMZ ash and blended ash, which had a high glass-forming ability (GFA). The slag formed at a high temperature had a higher polymerization degree and viscosity, which led to a decrease in the migration ability between ions, and ultimately made the slag difficult to crystallize during the cooling. When the proportion of IS was higher than 60%, the addition of IS increased the CaO and FeO content in the system. As network modifiers, CaO and FeO could provide O2− at a high temperature, which reacted with silicate network structure and continuously destroyed the complexity of network structure, thus reducing the polymerization degree and viscosity of slag. At this time, the migration ability between ions was enhanced, and needle-shaped/rod-shaped crystals were precipitated during the cooling process. Finally, the viscosity calculated by simulation and Einstein-Roscoe empirical formula demonstrated that the addition of IS could significantly improve the fluidity of coal ash and meet the requirements of the liquid slag-tapping gasifier. The purpose of this work was to provide theoretical support for slag flow mechanisms during the gasifier slagging-tapping process and the resource treatment of industrial solid waste.
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