煤气化细渣高真空脱水规律:滤饼裂纹演化、能耗优化与全生命周期评价

High-vacuum dewatering behaviors of coal gasification fine slag: Filter cake cracking evolution, energy consumption optimization, and life cycle assessment

  • 摘要: 为阐明物理化学结构特征与黑水固体质量分数引起的浆体堆积行为变化对煤气化细渣(Coal Gasification Fine Slag, CGFS)真空脱水性能的协同影响机制,选取陕西榆林地区2种代表性细渣(样品JYHG和YK2),在固体质量分数为6%~15%的条件下开展了系统的脱水过程试验。通过多尺度表征分析颗粒级配、孔结构及滤饼裂纹演化对脱水行为的耦合作用,并结合能耗分析与生命周期评价(Life Cycle Assessment, LCA)评估不同黑水固体质量分数条件下的经济性与环境效应。结果表明:颗粒较粗、孔隙结构复杂(分形维数D2为2.838)的样品JYHG易形成疏松滤饼,孔内水滞留严重;细颗粒含量高、堆积密度大的样品YK2在低固体质量分数下脱水性能较优,但在固体质量分数高(≥15%)时滤饼因毛细收缩应力剧增而产生宏观裂纹。这些裂纹诱发了严重的空气穿透现象,导致真空驱动力失效,滤饼含水率升高。滤饼裂纹率与最终含水率呈显著正相关,裂纹演化是高固体质量分数条件下脱水恶化的主导因素。能耗与 LCA 分析显示,提高黑水固体质量分数可显著降低单位干基气化渣处理能耗与温室气体排放,但固体质量分数过高会放大单位水处理能耗及人类健康毒性负荷。综合脱水效率、滤饼结构稳定性、能耗与环境影响,固体质量分数为10%~12%的黑水脱水,可在降低温室效应的同时,避免健康毒性与填埋风险的过度累积,并可有效提高脱水效率。研究明确了气化细渣脱水过程的“结构−能耗−环境”耦合机制,为煤化工固废的低碳高效处置提供了理论依据。

     

    Abstract: To elucidate the synergistic effects of physicochemical structural characteristics and the changes in black water deposition behavior caused by black water solid mass fractions on the vacuum dewatering performance of coal gasification fine slag (CGFS), 2 representative fine slags (samples JYHG and YK2) from Yulin, Shaanxi, were selected for systematic dewatering experiments within the solid mass fraction range of 6%−15%. Multiscale characterization techniques were used to analyze the coupled effects of particle gradation, pore structure, and filter cake crack evolution on dewatering behavior. Additionally, energy consumption analysis and life cycle assessment (LCA) were conducted to evaluate the economic and environmental performance under different solid mass fractions conditions. The results show that JYHG, characterized by coarser particles and a complex pore structure (fractal dimension D2 is 2.838), tends to form loose filter cakes with severe intraparticle water retention. YK2, with a higher proportion of fine particles and greater packing density, exhibits better dewatering performance at low solid mass fractions. However, at high solid mass fractions (≥15%), the filter cake undergoes macroscopic cracking due to the dramatic increase in capillary shrinkage stress. These cracks lead to severe air penetration, causing the vacuum driving force to fail and resulting in an increase in water content. A significant positive correlation was observed between the crack ratio and water content, with crack evolution being the dominant factor leading to dewatering deterioration at high solid mass fractions. Energy consumption and LCA analyses indicate that increasing the black water solid mass fractions significantly reduces the energy consumption per unit mass of dry CGFS and greenhouse gas emissions. However, excessively high solid mass fractions exacerbate the energy consumption per unit water treated and the human health toxicity burden. Considering dewatering efficiency, filter cake structural stability, energy consumption, and environmental impacts, a black water solid mass fraction of 10%−12% is identified as the optimal range for dewatering, which reduces the greenhouse effect while preventing excessive accumulation of health toxicity and landfill risks under high solid mass fraction conditions. This study clarifies the coupled “structure-energy-environment” mechanism governing CGFS dewatering and provides theoretical guidance for low-carbon and efficient disposal of coal chemical solid waste.

     

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