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煅燒因素對煤矸石煅燒產品白度及活性的影響

Effect of calcined factors on the whiteness and activity of calcined coal gangue products

  • 摘要: 煤矸石的大量堆存帶來了一系列的生產安全隱患和環境污染問題. 煅燒活化技術為實現煤矸石中有用元素和礦物的高質高效利用開辟了新途徑,但目前煅燒因素對煤矸石白度及火山灰活性的影響缺乏系統研究. 通過考察煅燒因素對煅燒煤矸石白度及火山灰活性的影響,探明了煤矸石煅燒前后物相組成、微觀形貌、孔徑分布、白度及火山灰活性的變化. 結果表明,動態煅燒產品的白度值及火山灰活性高于靜態煅燒產品. 在煅燒溫度為600~900 ℃、煅燒時間為2 h時,靜態煅燒產品的白度值增加幅度高于動態煅燒產品,隨著煅燒時間的延長,白度值持續增加. 相較于靜態煅燒,動態煅燒的燒結現象不明顯. 所得動態煅燒產品的比表面積、孔結構特征均優于靜態煅燒產品. 所得最佳煤矸石煅燒產品的煅燒方式為動態煅燒,煅燒溫度900 ℃,煅燒時間2 h.

     

    Abstract: Coal gangue (CG), a by-product of coal mining and processing, has long been considered problematic solid waste. Its large-scale disposal raises significant safety concerns and environmental issues. However, the current technologies for its harmless disposal and resource utilization remain inadequate. The performance of high-value CG products is suboptimal, market competitiveness is weak, and production costs are high. Additionally, the industry chain for high-value CG utilization is underdeveloped. To enhance CG resource utilization and improve environmental quality, developing effective treatment technologies has become an urgent priority for the coal industry. Calcination activation presents a promising approach to efficiently extract valuable elements and minerals from CG. However, a systematic understanding of the effects of calcination parameters on whiteness and pozzolanic activity of CG is still lacking. This study examines the effects of calcination methods, temperature, duration, heating rate, and particle size on the whiteness and pozzolanic activity of calcined CG products. By analyzing these factors, the study explores changes in the physical phase composition, micro-morphology, pore size distribution, whiteness, and pozzolanic activity of CG before and after calcination. Experimental results indicate that the optimal conditions for static calcination are a temperature of 900 ℃, a duration of 2 h, and a heating rate of 30 ℃·min–1. For dynamic calcination, the optimal conditions are a temperature of 900 ℃ and a duration of 2 h. The highest unit calcium absorption observed for the static calcined product is 1132.00, while for the dynamic calcined product, it is 1295.52. The dynamic calcined products exhibit superior whiteness and pozzolanic activity when compared to static calcined products. However, within the temperature range of 600–900 ℃ and a calcination time of 2 h, the whiteness of static calcined products increases more significantly than that of dynamic calcined products. Unlike dynamic calcination, the whiteness of static calcination continues to improve with prolonged calcination time. Additionally, dynamic calcination minimizes sintering effects and enhances the specific surface area and pore structure characteristics of the calcined products. With extended calcination time, the whiteness of calcined products continues to improve. Under identical calcination conditions, products with smaller particle sizes exhibit higher whiteness and pozzolanic activity. Dynamic calcination also effectively enhances the pozzolanic activity of CG. The heating rate and calcination time influence the degree of dehydroxylation of kaolinite, thereby affecting the pozzolanic activity of the calcined products. Furthermore, calcination methods impact heat transfer efficiency, oxygen diffusion, and decarbonization efficiency. This study provides theoretical and technical guidance for the high-value utilization of CG.

     

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