铁掺杂沸石包覆多孔粘土陶瓷膜(Fe/ZSM−5)的制备及其对重金属过滤机理的电化学研究

IF 5.4 Q2 ENGINEERING, ENVIRONMENTAL
Abdelrahman K.A. Khalil , Abderrazek El-kordy , Abdelaziz Elgamouz , Najib Tijani , Abdel-Nasser Kawde , Tahar Laoui , Salman S. Alharthi
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引用次数: 0

摘要

研究了Fe/ZSM−5沸石包覆多孔陶瓷膜(mZSM)的制备及其去除合成废水中重金属离子的性能。该膜是通过水热法合成的,利用掺有3wt . %活性炭(AC)的粘土载体来提高孔隙率。系统评价了Fe/ZSM−5包覆膜对Pb 2 +、Cd 2 +、Hg 2 +、Cu 2 +的过滤效果。扫描电镜显示棺材状或交错生长的Fe/ZSM−5晶体结构。XRD突出了7-9°和23-25°2θ的MFI框架反射,对应于(101)、(020)、(501)、(151)和(303)面。FTIR显示出典型的ZSM-5波段:401 cm⁻¹,590 cm⁻¹,679 cm⁻¹,781 cm⁻¹和1101 cm⁻¹。BET分析表明,其平均孔隙半径为1.704 nm,比表面积为251 m²/g,孔隙体积为0.214 cm³/g。mZSM膜表现出优异的HM去除效率,Cu 2 + (77.6%) <;Hg²+ (85.6%)<;Cd 2 + (95.1%) <;Pb 2 +(98.8%)优于未涂覆的粘土支撑体。水通量和渗透测试表明,粘土载体的初始纯水通量为199 L·m⁻²·h (LMH), 90分钟后稳定在144 LMH,而Fe/ZSM−5涂层膜由于缩小了孔径和增强了离子交换作用,其通量明显低于62.2 LMH。差分脉冲伏安法(DPV)的电化学研究证实,静电斥力在HM的吸附中起主导作用,而不是直接吸附。然而,金属在电极表面积累的顺序(Cd 2 + = 221 <;Pb 2 + = 447 <;Cu²+ = 654 μA <;Hg²+ = 667)与过滤顺序不同。这一差异表明,只有预处理电位才能解释HM在mZSM膜表面的污染机理。这些发现突出了Fe/ZSM−5改性膜在工业废水处理中的潜力,具有高截留率和可持续性能。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Preparation of Iron doped Zeolite-coated porous clay ceramic membrane (Fe/ZSM−5) for heavy metal filtration: Electrochemical study of the rejection mechanism

Preparation of Iron doped Zeolite-coated porous clay ceramic membrane (Fe/ZSM−5) for heavy metal filtration: Electrochemical study of the rejection mechanism
This study investigates the fabrication and performance of Fe/ZSM−5 zeolite-coated porous ceramic membranes (mZSM) for the removal of heavy metal (HM) ions from synthetic wastewater. The membrane was synthesized via a hydrothermal process, utilizing a clay support doped with 3 wt. % activated carbon (AC) to enhance porosity. The effectiveness of the Fe/ZSM−5-coated membrane in rejecting Pb²⁺, Cd²⁺, Hg²⁺, and Cu²⁺ ions was systematically evaluated. SEM reveals coffin-like or intergrown Fe/ZSM−5 crystal structures. XRD highlights MFI framework reflections at 7–9° and 23–25° 2θ, corresponding to the (101), (020), (501), (151), and (303) planes. FTIR displays characteristic ZSM-5 bands at 401 cm⁻¹, 590 cm⁻¹, 679 cm⁻¹, 781 cm⁻¹, and 1101 cm⁻¹. BET analysis shows a smaller average pore radius of 1.704 nm, a higher surface area of 251 m²/g, and a larger pore volume of 0.214 cm³/g. The mZSM membrane demonstrated superior HM removal efficiencies in the order of Cu²⁺ (77.6 %) < Hg²⁺ (85.6 %) < Cd²⁺ (95.1 %) < Pb²⁺ (98.8 %), outperforming the uncoated clay support. Water flux and permeation tests showed that the initial pure water flux of the clay support was 199 L·m⁻²·h⁻¹ (LMH), stabilizing at 144 LMH after 90 min, while the Fe/ZSM−5-coated membrane exhibited a significantly lower flux of 62.2 LMH due to reduced pore size and enhanced ion-exchange interactions. Electrochemical studies using Differential Pulse Voltammetry (DPV) confirmed that electrostatic repulsion played a dominant role in HM rejection rather than direct adsorption. However, the order of metal accumulation on the electrode surface (Cd²⁺ = 221 < Pb²⁺ = 447 < Cu²⁺ = 654 μA < Hg²⁺ = 667) differed from the filtration order. This discrepancy suggests that only the preconditioning potential can elucidate the fouling mechanism of HM at the mZSM membrane surface. These findings highlight the potential of Fe/ZSM−5-modified membranes for industrial wastewater treatment, offering high rejection rates and sustainable performance.
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来源期刊
Journal of hazardous materials advances
Journal of hazardous materials advances Environmental Engineering
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