首页> 外文期刊>Desalination and water treatment >Degradation of Ortho-Toluidine in petrochemical wastewater by ozonation, UV/O-3, O-3/H2O2 and UV/O-3/H2O2 processes
【24h】

Degradation of Ortho-Toluidine in petrochemical wastewater by ozonation, UV/O-3, O-3/H2O2 and UV/O-3/H2O2 processes

机译:臭氧氧化,UV / O-3,O-3 / H2O2和UV / O-3 / H2O2工艺降解石油化工废水中的邻甲苯胺

获取原文
获取原文并翻译 | 示例
       

摘要

In this research, degradation of Ortho-Toluidine (OT) that is considered toxic and carcinogenic in the wastewater of petrochemical industries was investigated by advanced oxidation processes in circulating photoreactor. The effect of some operational parameters such as pH, flow rates of ozone, dosage of the OT, and concentration of hydrogen peroxide pollutant was investigated. The degradation and relative mineralization of the OT were estimated by HPLC and COD tests, respectively. Optimal conditions were determined by using a factor at the time. The maximum reduction in COD was 57 and 70.2% for ozonation (initial pH 9) and UV/O-3 (initial pH of 11), respectively. In H2O2/O-3 (initial pH 9, initial concentration of H2O2 = 40 mM) and UV/O-3/H2O2 processes (initial pH of 10, initial concentration of H2O2 = 20 mM), 65.5 and 82.5% of COD removed, respectively. Reaction time for COD removal of OT solution in all processes was 120 min. Optimal dosage of ozone was 0.5 l/min for all processes based on ozone. Also, after 40 min of reaction, the degradation percent of OT was 100, 90.7, 89.5, and 85.5% for UV/O-3/H2O2, UV/O-3, O-3/H2O2, and O-3 processes, respectively. The optimum concentration of the OT was obtained at 100 mg/l in all processes. From the kinetic study, it was clear that the mineralization was slower than the degradation and the best process was the UV/O-3/H2O2, since it achieved the highest degradation and mineralization efficiency.
机译:在这项研究中,通过循环光反应器中的高级氧化工艺,研究了在石油化工行业废水中被认为有毒和致癌的邻甲苯胺(OT)的降解。研究了某些操作参数(例如pH值,臭氧流速,OT的剂量和过氧化氢污染物的浓度)的影响。 OT的降解和相对矿化分别通过HPLC和COD测试估算。通过使用当时的因素确定最佳条件。臭氧化(初始pH为9)和UV / O-3(初始pH为11)时,COD的最大减少分别为57%和70.2%。在H2O2 / O-3(初始pH 9,H2O2初始浓度= 40 mM)和UV / O-3 / H2O2工艺(初始pH 10,H2O2初始浓度= 20 mM)中,去除了65.5和82.5%的COD , 分别。在所有过程中,用于去除OT溶液的COD的反应时间为120分钟。对于所有基于臭氧的过程,最佳的臭氧剂量为0.5 l / min。同样,在反应40分钟后,对于UV / O-3 / H2O2,UV / O-3,O-3 / H2O2和O-3工艺,OT的降解百分比分别为100、90.7、89.5和85.5%,分别。在所有过程中,OT的最佳浓度均为100 mg / l。从动力学研究中可以清楚地看出,矿化比降解要慢,而最佳工艺是UV / O-3 / H2O2,因为它实现了最高的降解和矿化效率。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号