Ibrahim Yazan, Abdulkarem Elham, Naddeo Vincenzo, Banat Fawzi, Hasan Shadi W
Center for Membrane and Advanced Water Technology (CMAT), Department of Chemical Engineering, Khalifa University of Science and Technology, Masdar City Campus, P.O. Box 127788, Abu Dhabi, United Arab Emirates.
Department of Civil Engineering, University of Salerno, Via Giovanni Paolo II #132, 84084 Fisciano, SA, Italy.
Sci Total Environ. 2019 Nov 10;690:167-180. doi: 10.1016/j.scitotenv.2019.07.009. Epub 2019 Jul 3.
In this study, commercial cellulose membranes were surface coated with alpha‑zirconium phosphate nanoparticles (α-ZrP-n) to study their impact on the overall removal efficiency of heavy metals from synthetic metal mixture wastewater solution. A total of four homogeneous solutions (0.25, 0.50, 0.75, and 1.00 wt%) of α-ZrP-n were prepared by sonicating the nanoparticles in deionized water. These solutions were used to surface coat the commercial cellulose membranes. The Scanning Electron Microscopy (SEM) along with Energy Dispersive Spectroscopy (EDS) were used to confirm the attachment of α-ZrP-n on the cellulose membrane surface. Furthermore, the structural characteristics of the α-ZrP-n modified cellulose membranes were also studied. The water contact angle results showed that all coated membranes remained super-hydrophilic. The porosity of the membranes decreased to 48% with the addition of 1.00 wt% α-ZrP-n compared to 65% for the pristine membrane. The mechanical strength has improved from 3.4 MPa for the pristine membrane to about 4 MPa for the 1.00 wt% α-ZrP-n membrane. Similarly, the thermal stability was found to be slightly enhanced as evidenced by the increase in decomposition temperature to 280 and 285 °C in the 0.75 and 1.00 wt% α-ZrP-n membranes, respectively. Furthermore, a removal efficiency of 97.0 ± 0.6, 98.0 ± 0.5, 99.5 ± 0.2, and 91.5 ± 2.0% for Cu (II), Zn (II), Ni (II), and Pb (II), respectively, was observed with the 0.50 wt% α-ZrP-n membrane. This removal was achieved at a flux of 41.85 ± 0.87 × 10 LMH. Increasing the α-ZrP-n concentration further did not show any improvement in the overall removal efficiency. However, it led to 46% flux reduction in the 1.00 wt% α-ZrP-n membrane. The mechanism of removal of the heavy metal ions was postulated to be a combination of ion exchange and electrostatic attraction of the strong negatively charged α-ZrP-n membranes and the free metal ions in the wastewater solution.
在本研究中,对商用纤维素膜进行了磷酸锆纳米颗粒(α-ZrP-n)表面涂层处理,以研究其对合成金属混合废水溶液中重金属整体去除效率的影响。通过在去离子水中超声处理纳米颗粒,制备了总共四种α-ZrP-n的均匀溶液(0.25、0.50、0.75和1.00 wt%)。这些溶液用于对商用纤维素膜进行表面涂层处理。使用扫描电子显微镜(SEM)和能谱仪(EDS)来确认α-ZrP-n附着在纤维素膜表面。此外,还研究了α-ZrP-n改性纤维素膜的结构特性。水接触角结果表明,所有涂层膜均保持超亲水性。与原始膜的65%相比,添加1.00 wt%α-ZrP-n后膜的孔隙率降至48%。机械强度从原始膜的3.4 MPa提高到1.00 wt%α-ZrP-n膜的约4 MPa。同样,热稳定性略有提高,0.75和1.00 wt%α-ZrP-n膜的分解温度分别提高到280和285°C,证明了这一点。此外,0.50 wt%α-ZrP-n膜对Cu(II)、Zn(II)、Ni(II)和Pb(II)的去除效率分别为97. ± 0.6%、98.0 ± 0.5%、99.5 ± 0.2%和91.5 ± 2.0%。这种去除是在41.85 ± 0.87×10 LMH的通量下实现的。进一步提高α-ZrP-n浓度并未使整体去除效率有任何提高。然而,这导致1.00 wt%α-ZrP-n膜的通量降低了46%。重金属离子的去除机制被假定为带强负电荷的α-ZrP-n膜与废水溶液中的游离金属离子之间的离子交换和静电吸引的组合。