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    基于TG-MS/FTIR的煤矸石与污泥共热解特性研究

    Co-pyrolysis Characteristics of Coal Gangue and Sludge by TG-MS/FTIR

    • 摘要: 煤炭开采造成的煤矸石堆积会增加生态环境风险。热解技术以其清洁高效的处理特性,成为煤矸石资源化研究的热点之一。本文探讨了有机污泥与煤矸石的共热解,作为提升煤矸石热解特性和实现资源化利用的有效方法。通过热重质谱红外(TG-MS/FTIR)三联用方法,研究了煤矸石与工业有机污泥混合共热解过程的热分解特性、动力学特性、挥发分分布及其相互作用。结果表明,污泥和煤矸石的混合热解存在显著的协同效应。煤矸石与污泥混合共热解包括第一阶段(210~410 ℃)和第二阶段(410~584 ℃)。混合物热重曲线实验值与理论值的差异均为负值,表明共热解过程中存在协同促进作用。同时,热解性能参数的计算结果显示,污泥的掺入显著提升了混合物的热解性能。通过3种热解动力学模型计算,煤矸石和污泥的活化能分别为314.00~321.55 kJ/mol和236.13~240.73 kJ/mol。数据对比发现,污泥的掺混有效降低了混合物热解所需的活化能。傅里叶红外光谱(FTIR)分析表明,具有高灰分特性的煤矸石在热解过程中几乎未产生明显的挥发分,而煤矸石中的金属矿物与污泥挥发分的相互作用促进了C2H2 +、C3H5 +和C3H7 +等轻烃小分子的产生。研究结果表明,煤矸石与污泥的共热解提升了热解性能,降低了反应活化能,同时还增加了气体产物的生成,为煤矸石的热解资源化提供了有价值的参考。

       

      Abstract: The accumulation of coal gangue, a major solid waste generated from coal mining, poses increasingly severe environmental and ecological risks, including soil contamination, water pollution, and landscape degradation. As an advanced thermal conversion technology, pyrolysis has emerged as a promising approach for coal gangue valorization due to its clean disposal, high efficiency, and minimal secondary pollution. Among various strategies, the co-pyrolysis of industrial sewage sludge with coal gangue is considered an effective route to improve the pyrolysis characteristics of coal gangue and achieve synergistic solid waste utilization. In this study, coupled thermogravimetry–mass spectrometry (TG-MS) and Fourier transform infrared spectroscopy (FTIR) were employed to investigate the thermal decomposition behavior, kinetic parameters, volatile distribution, and interactions during the co-pyrolysis process, enabling real-time monitoring and comprehensive reaction analysis. The results revealed a distinct synergistic effect during co-pyrolysis. Specifically, the main thermal decomposition consisted of two distinct stages: a primary stage (210–410 °C) dominated by the decomposition of light organic fractions in the sludge, and a secondary stage (410–584 °C) driven by the cracking of heavy organic matter from both feedstocks. Notably, the difference between experimental and theoretical thermogravimetric (TG) curves was negative, serving as direct evidence of synergy. Furthermore, key pyrolysis evaluation parameters confirmed that sludge addition effectively enhanced overall thermochemical reactivity. Kinetics were evaluated using Kissinger–Akahira–Sunose, Ozawa–Flynn–Wall, and Starink models. The calculated activation energies for individual coal gangue and sludge ranged from 314.00 to 321.55 kJ/mol and 236.13 to 240.73 kJ/mol, respectively, whereas co-pyrolysis significantly reduced the overall activation energy, thereby lowering the energy barrier for thermal degradation. Additionally, FTIR and MS results demonstrated that while coal gangue produced negligible volatile products owing to its high ash content, the interaction between metallic minerals in coal gangue and the volatile matter released from sludge markedly promoted the formation of light hydrocarbons (e.g., C2H2 +, C3H5 +, and C3H7 + fragments). In conclusion, this work demonstrates that co-pyrolysis with industrial sewage sludge enhances thermochemical conversion performance, lowers activation energy barriers, and increases high-value gas yields, providing valuable theoretical insights and technical support for coal gangue resource recovery.

       

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