Ingeniería Química, Facultad de Ciencias, Universidad Autónoma de Madrid Ctra de Colmenar km 15, 28049 Madrid, Spain.
J Hazard Mater. 2013 May 15;252-253:180-5. doi: 10.1016/j.jhazmat.2013.02.042. Epub 2013 Mar 1.
This work investigates the application of Fenton process to the treatment of a highly polluted industrial wastewater resulting from the pipeline cleaning in a power plant. This effluent is characterized by a high chemical oxygen demand (COD>40 g/L), low biodegradability and quite a high iron concentration (around 3g/L) this coming from pipeline corrosion. The effect of the initial reaction temperature (between 50 and 90 °C) and the way of feeding H2O2 on the mineralization percentage and the efficiency of H2O2 consumption has been analyzed. With the stoichiometric amount of H2O2 relative to initial COD, fed in continuous mode, more than 90% COD reduction was achieved at 90 °C. That was accompanied by a dramatic improvement of the biodegradability. Thus, a combined treatment based on semicontinuous high-temperature Fenton oxidation (SHTF) and conventional aerobic biological treatment would allow fulfilling the COD and ecotoxicity regional limits for industrial wastewaters into de municipal sewer system. For the sake of comparison, catalytic wet air oxidation was also tested with poor results (less than 30% COD removal at 140 °C and 8 atm oxygen pressure).
本研究采用芬顿工艺处理来自电厂管道清洗的高污染工业废水。该废水具有化学需氧量(COD>40 g/L)高、生物可降解性低和铁浓度(约 3g/L)高的特点,这是由于管道腐蚀所致。分析了初始反应温度(50 至 90°C)和 H2O2 进料方式对矿化率和 H2O2 消耗效率的影响。采用化学计量的 H2O2 与初始 COD 反应,在连续模式下进料,在 90°C 时可实现超过 90%的 COD 去除率。这伴随着生物降解性的显著提高。因此,基于高温半连续芬顿氧化(SHTF)和传统好氧生物处理的组合处理将允许满足工业废水进入城市下水道系统的 COD 和生态毒性区域限值。为了进行比较,还测试了催化湿式空气氧化,但效果不佳(在 140°C 和 8 大气压氧气压力下,COD 去除率小于 30%)。