Rezaei Mohammad, Rashidi Fariborz, Royaee Sayed Javid, Jafarikojour Morteza
Chemical Engineering Department, Amirkabir University of Technology, Tehran, Iran.
Environ Sci Pollut Res Int. 2014 Nov;21(21):12505-17. doi: 10.1007/s11356-014-3166-3. Epub 2014 Jun 20.
A novel photocatalytic reactor for wastewater treatment was designed and constructed. The main part of the reactor was an aluminum tube in which 12 stainless steel circular baffles and four quartz tube were placed inside of the reactor like shell and tube heat exchangers. Four UV-C lamps were housed within the space of the quartz tubes. Surface of the baffles was coated with TiO2. A simple method was employed for TiO2 immobilization, while the characterization of the supported photocatalyst was based on the results obtained through performing some common analytical methods such as X-ray diffraction (XRD), scanning electron microscope (SEM), and BET. Phenol was selected as a model pollutant. A solution of a known initial concentration (20, 60, and 100 ppmv) was introduced to the reactor. The reactor also has a recycle flow to make turbulent flow inside of the reactor. The selected recycle flow rate was 7 × 10(-5) m(3).s(-1), while the flow rate of feed was 2.53 × 10(-7), 7.56 × 10(-7), and 1.26 × 10(-6) m(3).s(-1), respectively. To evaluate performance of the reactor, response surface methodology was employed. A four-factor three-level Box-Behnken design was developed to evaluate the reactor performance for degradation of phenol. Effects of phenol inlet concentration (20-100 ppmv), pH (3-9), liquid flow rate (2.53 × 10(-7)-1.26 × 10(-6) m(3).s(-1)), and TiO2 loading (8.8-17.6 g.m(-2)) were analyzed with this method. The adjusted R (2) value (0.9936) was in close agreement with that of corresponding R (2) value (0.9961). The maximum predicted degradation of phenol was 75.50 % at the optimum processing conditions (initial phenol concentration of 20 ppmv, pH ∼ 6.41, and flow rate of 2.53 × 10(-7) m(3).s(-1) and catalyst loading of 17.6 g.m(-2)). Experimental degradation of phenol determined at the optimum conditions was 73.7 %. XRD patterns and SEM images at the optimum conditions revealed that crystal size is approximately 25 nm and TiO2 nanoparticles with visible agglomerates distribute densely and uniformly over the surface of stainless steel substrate. BET specific surface area of immobilized TiO2 was 47.2 and 45.8 m(2) g(-1) before and after the experiments, respectively. Reduction in TOC content, after steady state condition, showed that maximum phenol decomposition occurred at neutral condition (pH ∼ 6).
设计并构建了一种用于废水处理的新型光催化反应器。该反应器的主要部分是一根铝管,其中12个不锈钢圆形折流板和4根石英管像管壳式换热器一样放置在反应器内部。4个紫外线C灯安装在石英管的空间内。折流板表面涂覆有二氧化钛。采用了一种简单的方法固定二氧化钛,而负载型光催化剂的表征基于通过执行一些常见分析方法(如X射线衍射(XRD)、扫描电子显微镜(SEM)和BET)获得的结果。选择苯酚作为模型污染物。将已知初始浓度(20、60和100 ppmv)的溶液引入反应器。该反应器还具有循环流,以使反应器内部形成湍流。选定的循环流速为7×10⁻⁵ m³·s⁻¹,而进料流速分别为2.53×10⁻⁷、7.56×10⁻⁷和1.26×10⁻⁶ m³·s⁻¹。为了评估反应器的性能,采用了响应面法。开发了一种四因素三水平的Box-Behnken设计,以评估反应器对苯酚降解的性能。用该方法分析了苯酚入口浓度(20 - 100 ppmv)、pH值(3 - 9)、液体流速(2.53×10⁻⁷ - 1.26×10⁻⁶ m³·s⁻¹)和二氧化钛负载量(8.8 - 17.6 g·m⁻²)的影响。调整后的R²值(0.9936)与相应的R²值(0.9961)非常接近。在最佳工艺条件下(初始苯酚浓度为20 ppmv、pH值约为6.41、流速为2.53×10⁻⁷ m³·s⁻¹和催化剂负载量为17.6 g·m⁻²),预测的苯酚最大降解率为75.50%。在最佳条件下测定的苯酚实验降解率为73.7%。最佳条件下的XRD图谱和SEM图像显示,晶体尺寸约为25 nm,带有可见团聚体的二氧化钛纳米颗粒密集且均匀地分布在不锈钢基材表面。实验前后负载型二氧化钛的BET比表面积分别为47.2和45.8 m²·g⁻¹。稳态条件后总有机碳含量的降低表明,苯酚在中性条件(pH值约为6)下分解最大。