Research Center for Biochemical and Environmental Engineering, Department of Applied Chemistry, Toyo University, 2100 Kujirai, Kawagoe, Saitama 350-8585, Japan.
Research Center for Biochemical and Environmental Engineering, Department of Applied Chemistry, Toyo University, 2100 Kujirai, Kawagoe, Saitama 350-8585, Japan.
J Environ Manage. 2014 Jun 15;139:172-9. doi: 10.1016/j.jenvman.2014.02.032. Epub 2014 Apr 1.
The degradation of model dark brown colored coffee effluent using photocatalyst zinc oxide (ZnO) has been systematically studied by varying ZnO dosage from 0 to 4000 mg L(-1), coffee loading from 0 to 90 mg L(-1) and intensity of UV light having the radiation peak at 352 nm from 0 to 18 W(m-lamp length)(-1). Almost complete decolorization was achieved after 180 min for the initial coffee concentration of 50 mg L(-1) with ZnO dosage of 3000 mg L(-1) and three UV lamps. The dissolved oxygen (DO) largely affected the photodecolorization process. Without air sparging or with oxygen supply only through the free-surface, the DO concentration significantly decreased during the initial decolorization process and then increased to the saturated DO concentration after about 80% decolorization was achieved. Under the anoxic condition with nitrogen gas sparging, the efficient color removal was not obtained unlike the decolorization without air sparging or under the oxic condition with air sparging. These findings suggest that the change in DO concentration was controlled by the oxygen consumption for the formation of oxygen adduct intermediates such as organoperoxy radicals. The mineralization rate of model coffee effluent was rather slow as compared with the decolorization rate and it was insignificantly affected by anoxic and oxic conditions. The present results indicate that ZnO photocatalyst has potential for treatment of coffee processing wastewaters.
使用光催化剂氧化锌(ZnO)对模型深棕色咖啡废水进行了系统降解研究,通过改变 ZnO 用量(0 至 4000 mg L(-1))、咖啡负载量(0 至 90 mg L(-1))和 352nm 辐射峰的紫外光强度(0 至 18 W(m-灯长)(-1))。对于初始浓度为 50 mg L(-1)的咖啡废水,在 ZnO 用量为 3000 mg L(-1)和三个紫外灯的条件下,经过 180 分钟几乎可以完全脱色。溶解氧(DO)对光脱色过程有很大影响。在没有曝气或仅通过自由表面供氧的情况下,DO 浓度在初始脱色过程中显著下降,然后在达到约 80%的脱色率后增加到饱和 DO 浓度。在充氮气的缺氧条件下,与没有曝气或曝气的有氧条件下的脱色情况不同,无法获得有效的颜色去除效果。这些发现表明,DO 浓度的变化受氧消耗的控制,这是形成氧加合物中间体(如有机过氧自由基)所必需的。与脱色速率相比,模型咖啡废水的矿化速率相当缓慢,缺氧和有氧条件对其影响不大。目前的结果表明,ZnO 光催化剂具有处理咖啡加工废水的潜力。