Department of Chemical and Nuclear Engineering, Universitat Politècnica de València, Camino de Vera s/n, 46022 Valencia, Spain.
J Hazard Mater. 2012 Mar 30;209-210:492-500. doi: 10.1016/j.jhazmat.2012.01.065. Epub 2012 Jan 28.
An ultrafiltration (UF) ceramic membrane was used to decolorize Reactive Black 5 (RB5) solutions at different dye concentrations (50 and 500 mg/L). Transmembrane pressure (TMP) and cross-flow velocity (CFV) were modified to study their influence on initial and steady-state permeate flux (J(p)) and dye rejection (R). Generally, J(p) increased with higher TMP and CFV and lower feed concentration, up to a maximum steady-state J(p) of 266.81 L/(m(2)h), obtained at 3 bar, 3m/s and 50mg/L. However, there was a TMP value (which changed depending on operating CFV and concentration) beyond which slight or no further increase in steady-state J(p) was observed. Similarly, the higher the CFV was, the more slightly the steady-state J(p) increased. Furthermore, the effectiveness of ultrafiltration treatment was evaluated through dye rejection coefficient. The results showed significant dye removals, regardless of the tested conditions, with steady-state R higher than 79.8% for the 50mg/L runs and around 73.2% for the 500 mg/L runs. Finally response surface methodology (RSM) was used to optimize membrane performance. At 50mg/L, a TMP of 4 bar and a CFV of 2.53 m/s were found to be the conditions giving the highest steady-state J(p), 255.86 L/(m(2)h), and the highest R, 95.2% simultaneously.
采用超滤(UF)陶瓷膜对不同染料浓度(50 和 500mg/L)的活性黑 5(RB5)溶液进行脱色。改变跨膜压力(TMP)和错流速度(CFV),研究其对初始和稳态渗透通量(J(p))和染料截留率(R)的影响。一般来说,J(p)随 TMP 和 CFV 的升高以及进料浓度的降低而升高,在 3 巴、3m/s 和 50mg/L 下达到最大稳态 J(p)266.81L/(m(2)h)。然而,存在一个 TMP 值(取决于操作 CFV 和浓度),超过该值后,稳态 J(p)仅略有增加或不再增加。同样,CFV 越高,稳态 J(p)的增加越轻微。此外,通过染料截留系数评估超滤处理的效果。结果表明,无论测试条件如何,染料去除率均显著,稳态 R 对于 50mg/L 运行高于 79.8%,对于 500mg/L 运行约为 73.2%。最后,采用响应面法(RSM)优化膜性能。在 50mg/L 时,发现 TMP 为 4 巴,CFV 为 2.53m/s 是获得最高稳态 J(p)255.86L/(m(2)h)和最高 R95.2%的条件。