State Environmental Protection Key Laboratory of Environmental Risk Assessment and Control on Chemical Process, East China University of Science and Technology, No. 130, Meilong Road, Shanghai 200237, China.
J Hazard Mater. 2010 Apr 15;176(1-3):1051-7. doi: 10.1016/j.jhazmat.2009.11.147. Epub 2009 Dec 3.
The degradation of clofibric acid (CA) in UV(254)/H(2)O(2) process under three temperature ranges, i.e. T1 (9.0-11.5 degrees C), T2 (19.0-21.0 degrees C) and T3 (29.0-30.0 degrees C) was investigated. The effects of solution constituents including NO(3)(-) and HCO(3)(-) anions, and humic acid (HA) on CA degradation were evaluated in Milli-Q waters. CA degradation behaviors were simulated with the pseudo-first-order kinetic model and the apparent rate constant (k(ap)) and half-life time (t(1/2)) were calculated. The results showed that higher temperature would favor CA degradation, and CA degradation was taken place mostly by indirect oxidation through the formation of OH radicals in UV(254)/H(2)O(2) process. In addition, the effects of both NO(3)(-) and HCO(3)(-) anions at two selected concentrations (1.0x10(-3) and 0.1 mol L(-1)) and HA (20 mg L(-1)) on CA degradation were investigated. The results showed that HA had negative effect on CA degradation, and this effect was much more apparent under low temperature condition. On the other hand, the inhibitive effect on CA degradation at both lower and higher concentrations of bicarbonate was observed, and this inhibitive effect was much more apparent at higher bicarbonate concentration and lower temperature condition. While, at higher nitrate concentration the inhibitive effect on CA degradation under three temperature ranges was observed, and with the temperature increase this negative effect was apparently weakened. However, at lower nitrate concentration a slightly positive effect on CA degradation was found under T2 and T3 conditions. Moreover, when using a real wastewater treatment plant (WWTP) effluent spiked with CA over 99% of CA removal could be achieved under 30 degrees C within only 15 min compared with 40 and 80 min under 20 and 10 degrees C respectively, suggesting a significant promotion in CA degradation under higher temperature condition. Therefore, it can be concluded that temperature plays an important role in CA degradation in UV/H(2)O(2) process.
在三个温度范围(即 T1(9.0-11.5 摄氏度)、T2(19.0-21.0 摄氏度)和 T3(29.0-30.0 摄氏度))下,研究了在 UV(254)/H(2)O(2)过程中,氯菲酸(CA)的降解情况。在 Milli-Q 水中评估了溶液成分(包括 NO(3)(-)和 HCO(3)(-)阴离子以及腐殖酸(HA))对 CA 降解的影响。用拟一级动力学模型模拟 CA 降解行为,并计算表观速率常数(k(ap))和半衰期(t(1/2))。结果表明,较高的温度有利于 CA 的降解,并且 CA 的降解主要是通过在 UV(254)/H(2)O(2)过程中形成 OH 自由基的间接氧化来进行的。此外,还研究了在两个选定浓度(1.0x10(-3)和 0.1 mol L(-1))和 HA(20 mg L(-1))下,NO(3)(-)和 HCO(3)(-)阴离子以及 HA 对 CA 降解的影响。结果表明,HA 对 CA 的降解有负面影响,并且在低温条件下这种影响更为明显。另一方面,在较低和较高浓度的碳酸氢盐下观察到对 CA 降解的抑制作用,并且在较高的碳酸氢盐浓度和较低的温度条件下,这种抑制作用更为明显。然而,在较高的硝酸盐浓度下,在三个温度范围内观察到对 CA 降解的抑制作用,并且随着温度的升高,这种负面影响明显减弱。然而,在较低的硝酸盐浓度下,在 T2 和 T3 条件下发现对 CA 降解有轻微的正影响。此外,当使用真实的污水处理厂(WWTP)流出物时,在 30 摄氏度下仅需 15 分钟即可去除超过 99%的 CA,而在 20 摄氏度和 10 摄氏度下分别需要 40 分钟和 80 分钟,这表明在较高温度下 CA 的降解有显著的促进作用。因此,可以得出结论,温度在 UV/H(2)O(2)过程中 CA 的降解中起着重要的作用。