吉林大学学报(理学版) ›› 2025, Vol. 63 ›› Issue (3): 963-0972.

• • 上一篇    

铁系/污泥基生物炭催化剂的制备及性能

王飞1,2, 胡绍伟1,2, 马光宇1,2, 于梦琦3, 徐晓晨3   

  1. 1. 海洋装备用金属材料及其应用国家重点实验室, 辽宁 鞍山 114009;2. 鞍钢集团 钢铁研究院, 辽宁 鞍山 114009;3. 大连理工大学 环境学院, 辽宁 大连 116024
  • 收稿日期:2024-08-27 出版日期:2025-05-26 发布日期:2025-05-26
  • 通讯作者: 徐晓晨 E-mail:xxcep@dlut.edu.cn

Preparation and Properties of Iron/Sludge-Based Biochar Catalysts

WANG Fei1,2,  HU Shaowei1,2,  MA Guangyu1,2,  YU Mengqi3,  XU Xiaochen3   

  1. 1. State Key Laboratory of Metal Material  for Marine Equipment and Application,  Anshan 114009, Liaoning Province, China;  
    2. Iron and Steel Research Institute,  Anshan Iron and Steel Group,  Anshan 114009,  Liaoning Province, China; 3. School of Environmental Science and Technology,   Dalian University of Technology,  Dalian 116024, Liaoning Province, China
  • Received:2024-08-27 Online:2025-05-26 Published:2025-05-26

摘要: 为实现固体废物的综合再利用, 以辽宁省鞍山市某钢厂区污水处理段的活性污泥和Fenton铁泥混合泥为原料, 以无机物高岭土为黏结剂, 通过混合挤条和热解的方法制备铁系/污泥基生物炭催化剂, 对其结构进行表征,  并优化制备工艺条件. 以喹啉为目标污染物, 优化催化臭氧氧化降解喹啉模拟废水的工艺参数, 并研究催化剂的稳定性和催化机理.  实验结果表明: 催化剂表面粗糙且空隙结构丰富, 催化剂中主要有Fe3O4,CaCO3和ZrO2晶体; 催化剂的最佳制备条件为黏结剂添加量12.5%, 热解温度800 ℃, 热解时间3 h;   在初始pH=7, 催化剂投加量为50 g, 喹啉初始质量浓度为50 mg/L条件下, 反应10 min去除率达76.31%; 催化剂具有良好的稳定性, 连续使用5次后, 喹啉的去除率仅下降0.09个百分点; 该催化体系中存在羟基自由基(.OH)和超氧自由基(O.-2)两种自由基以及单线态氧(1O2)非自由基,其中O.-2在反应中起主导作用; 反应前后Fe2+/Fe3+的比例变化表明, Fe2+/Fe3+的氧化还原循环参与了催化降解反应. 该研究为固体废物再利用和焦化废水的高效处理提供新的思路和方法. 

关键词: Fenton铁泥, 生物污泥, 铁系/污泥基生物炭, 催化臭氧, 喹啉

Abstract: In order to realize the comprehensive reuse of solid waste,  the iron/sludge-based biochar catalyst  was prepared by using the mixed sludge of activated sludge and Fenton iron sludge from the sewage treatment section of steel plant in Anshan, Liaoning Province as raw materials, and kaolinite as binder by a mixing-extrusion and pyrolysis method. The structure was characterized and the preparation process conditions were optimized. We optimized the process parameters of catalytic ozonation degradation of simulated wastewater containing quinoline as the target pollutant, and studied the stability and catalytic mechanism of catalyst. The experimental results show that the surface of catalyst is rough with a rich porous structures, and the catalyst mainly contains Fe3O4,CaCO3 and ZrO2 crystals. The optimal preparation conditions for the catalyst are a binder addition of 12.5%, pyrolysis temperature of 800 ℃, and pyrolysis time of 3 h. Under the conditions of initial pH=7, catalyst dosage of 50 g,  and  initial mass concentration of 50 mg/L of quinoline, the removal rate reaches 76.31% after 10 min of reaction. The catalyst has good stability,  and the removal rate of quinoline only decreases by 0.09 percentage points  after continuous  use for five times. There are two types of   hydroxyl radical (.OH) and superoxide anion radical (O.-2), as well as singlet oxygen  (1O2) non  free radicals  in the catalytic system, with  O.-2   playing a dominant role in the reaction. The change of Fe2+/Fe3+ ratio before and after the reaction indicates that the redox cycle of Fe2+/Fe3+ participates in the catalytic degradation reaction. This study provides a new idea and method for the reuse of solid waste and the efficient treatment of coking wastewater.

Key words: Fenton iron sludge, activated sludge,  ,  , iron/sludge-based biochar,  , catalytic ozonation,  , quinoline

中图分类号: 

  • X756