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含酚类煤化工废水自还原Fe3+类芬顿体系研究OA北大核心CSTPCD

Study of Self-reducing Fe3+Fenton-like System for Phenol-containing Coal Chemical Wastewater

中文摘要英文摘要

煤化工废水水质复杂,难降解有机物及氨氮含量高,给废水处理带来较大难度.现有的煤化工废水处理技术(混凝法、吸附法、膜生物反应法等)具有成本高、运行不稳定、预处理效果差等缺陷,难以满足煤化工行业发展的需要.为了高效处理煤化工废水,本文利用煤化工废水中酚类有机物的还原性促进Fe3+/Fe2+的循环,提出了一种利用Fe3+/H2O2类芬顿体系处理煤化工废水的方法.实验结果表明:Fe3+/H2O2体系中COD、TOC、TN、NH3-N的去除率可以达到74.63%、52.62%、10.46%、15.11%;相比于其他体系,Fe3+/H2O2体系出水色度明显降低,UV-Vis光谱下降幅度最大,铁泥量也明显减少.Q-TOF分析结果表明:废水中主要的8种有机物为酚类或具有醛基、羰基、羧基、碳碳双键或者酯基等还原性的官能团.通过测定COD去除率和pH、Fe3+/Fe2+、H2O2等含量随时间的变化趋势,提出了Fe3+/H2O2体系去除有机物的机理:废水中的还原性有机物将Fe3+还原为Fe2+,促进Fe3+/Fe2+循环,生成的Fe2+与H2O2发生芬顿反应,实现废水中有机污染物的去除.利用控制变量法,确定了最佳运行工况为:Fe2(SO4)3添加量为1.0 g/L、H2O2添加量为50mmol/L、反应温度为30 ℃、初始pH为6.8.在此工况下,反应60 min后,煤化工废水的COD、TOC、TN、NH3-N去除效果良好,色度明显降低,BOD5和COD的比值(B/C)从0.17提升至0.47,可生化性大幅提高.本文证实了利用含酚类煤化工废水自还原Fe3+/H2O2体系的可行性,降低了运行成本,可为后续研究及工程应用提供理论基础.

Coal chemical wastewater exhibits complex water quality,with a high concentration of difficult-to-degrade organic matter and ammo-nia nitrogen,posing significant challenges for wastewater treatment.Current technologies,including coagulation,adsorption,and membrane bioreactors,have limitations such as high costs,unstable operation,and suboptimal pretreatment effects,failing to meet the evolving needs of the coal chemical industry.This study introduces a novel method using the reducibility of phenolic organic compounds in coal chemical wastewater to enhance the Fe3+/Fe2+cycle in the Fe3/H2O2 Fenton-like system,thus efficiently treating the wastewater.Comparative experiments demonstrated that the Fe3+/H2O2 system achieves removal rates of COD,TOC,TN,and NH3-N at 74.63%,52.62%,10.46%,and 15.11%,respectively.This system significantly reduces coloration,shows the largest decline in the UV-Vis spectrum,and decreases the amount of iron sludge.Q-TOF ana-lysis revealed that the primary eight organic compounds in the wastewater are phenolic or contain reducible functional groups such as aldehyde,carbonyl,carboxyl,carbon-carbon double bond,or ester.By monitoring changes in the COD removal rate and pH,Fe3+/Fe2+,H2O2,and others over time,the mechanism of organic matter removal in the Fe3+/H2O2 system is proposed:the reducible organic matter reduces Fe3+to Fe2+,en-hancing the Fe3+/Fe2+cycle,and the generated Fe2+reacts with H2O2 to remove organic pollutants via the Fenton reaction.Optimal operating con-ditions are identified as Fe2(SO4)3 dosage of 1.0 g/L,H2O2 dosage of 50 mol/L,reaction temperature of 30 ℃,and initial pH of 6.8 using the con-trolled variable method.Under these conditions,after 60 minutes,the treatment shows significant COD,TOC,TN,and NH3-N removal efficien-cies,a significant reduction in color,and an increase in biodegradability,with the B/C ratio rising from 0.17 to 0.47.This study confirms the viab-ility of using a self-reduction Fe3+/H2O2 system for phenolic coal chemical wastewater,reducing operating costs and providing a theoretical foundation for further research and engineering applications.

丛伯一;刘杨;殷浩翔;张恒;周鹏;李伟;赖波

四川大学建筑与环境学院,四川成都 610065四川大学化学工程学院,四川成都 610065中国五冶集团有限公司,四川成都 610063

环境科学

Fe3+H2O2类芬顿煤化工废水酚类化合物

Fe3+H2O2fenton-likecoal chemical wastewaterphenolic compounds

《工程科学与技术》 2024 (004)

57-65 / 9

国家自然科学基金青年基金项目(42107073)

10.15961/j.jsuese.202300391

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