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    废旧印刷线路板与废汽车催化剂共熔炼过程有机污染物演化机制

    Evolution of Organic Pollutants During Co-Smelting of Waste Printed Circuit Boards and Spent Automotive Catalysts

    • 摘要: 废旧印刷线路板(WPCBs)与废汽车催化剂(SACs)共熔炼技术,通过利用废旧印刷线路板中的铜资源,实现铜对金、银及铂族金属(PGMs)等关键战略金属的高效捕集与回收,开创了“以废制废”的循环利用新路径,为两类危险废物的资源化处理提供了有力支持。然而,该过程中有机污染物的迁移与转化机理尚需深入研究。基于前期确定的共熔炼优化条件(熔炼温度为1 400 ℃、保温时间4 h、捕集剂配比(质量分数)25%、碱度1.0),系统分析了废线路板与废汽车催化剂共熔炼过程中有机物的组分特征,深入探讨了污染物的生成途径与转化机理,并对其毒性进行综合评价。结果表明,共熔炼过程产生的液相组分主要为苯及苯酚同系物,其中苯含量约为35.77%,苯酚约为37.26%;气相成分主要为H2、芳香烃、CO、CH4和CO2等小分子物质;体系中PGMs可降低有机物分解活化能;液相和气相组分中毒性危害最显著的5类物质依次为4-苯基苯酚、双酚A、苯酚、萘及对甲苯酚。研究揭示了共熔炼过程污染物的生成与分解机制,为该技术的污染控制提供了参考。

       

      Abstract: The co-smelting of waste printed circuit boards (WPCBs) and spent automotive catalysts (SACs) represents an innovative "waste-to-resource" strategy for recovering resources from hazardous wastes. Through metallurgical interactions, the copper in WPCBs acts as an efficient scavenger for enriching platinum group metals (PGMs), gold, and silver from SACs. Although this technology provides a sustainable treatment solution for these hazardous wastes through the synergistic recovery of metals, the transformation mechanisms of organic pollutants during the co-smelting process are not well understood. This study systematically investigated the transformation behavior of organic pollutants under optimized metal recovery conditions: a smelting temperature of 1 400 ℃, a holding time of 4 h, a WPCBs-to-SACs ratio of 25%, and a basicity of 1.0. The chemical compositions of SACs and WPCBs was characterized using X-ray diffraction (XRD) and Fourier transform infrared spectroscopy (FTIR). Their elemental contents were determined by X-ray fluorescence spectrometry (XRF) and inductively coupled plasma optical emission spectrometry (ICP-OES). Subsequently, the liquid-phase and gas-phase products from the co-smelting process were collected to assess secondary pollution risks. Gas chromatography-mass spectrometry (GC-MS) was employed to identify the compostion of organic substances. The weight loss characteristics and pyrolysis mechanisms of the materials were further analyzed. The Kissinger-Akahira-Sunose (KAS), Flynn-Wall-Ozawa (FWO), and Friedman methods were used to study the kinetic mechanisms of organic substance decomposition during co-smelting. The reaction kinetic model equations were applied to fit different conversion rate intervals to explore the decomposition mechanisms of organic substances. Additionally, an equivalent weighting method was employed to comprehensively assess the product toxicity, bioaccumulation, persistence, and secondary pollution risks. Analysis of organic substance composition revealed that the liquid-phase products mainly consisted of benzene derivatives (35.77%) and phenolic derivatives (37.26%), with no halogenated pollutants detected. The gas-phase products were primarily composed of small molecules such as H2, CO, CH4, CO2, and aromatics. Therefore, the co-smelting process resulted in the dehalogenation and molecular weight reduction of the products, reducing environmental risks. The metal components in the WPCBs-SACs co-smelting system catalyzed the decomposition of epoxy resins in WPCBs. The metals inherently present in the co-smelting system (e.g., Cu, Fe, and PGMs) significantly reduced the activation energy for organic substance decomposition, promoting the efficient cracking of complex pollutants. Within the temperature range of 600−800 ℃, the activation energy for organic substance decomposition decreased by 221.64−286.64 kJ/mol. The comprehensive toxicity assessment identified 4-phenylphenol, bisphenol A, phenol, naphthalene, and p-cresol as the organic pollutants with the highest environmental risks in the gas and liquid phases. Building on previous research on the co-smelting recovery of PGMs from WPCBs and SACs, this study comprehensively elucidated the transformation mechanisms of organic pollutants during the smelting process.

       

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