Key Takeaways & Executive Findings
- •• Ar plasma treatment effectively enlarges the interlayer spacing of NiCoAl-LDHs, enhancing chloride ion diffusion and active site exposure. • The flexible carbon cloth substrate improves electrical conductivity and prevents nanosheet agglomeration, enabling self-supporting electrodes without binders. • The Ar-NiCoAl-LDHs@ACC electrode achieves a high salt removal capacity of 93.26 mg g−1 and a rapid rate of 0.27 mg g−1 s−1 at 1.2 V. • The electrode exhibits excellent cycling stability with over 85% capacity retention after 100 cycles, demonstrating practical potential for brackish water desalination.
Abstract
Capacitive deionization (CDI) has been regarded as an emerging desalination technology in recent years, especially for brackish water, due to its economic and energy-saving advantages. However, research on chloride removal electrodes is limited, and slow desalination kinetics also restrict their development. In this work, NiCoAl-LDHs nanosheet arrays were grown in situ on flexible carbon cloth (ACC) after surface acid treatment and then subjected to Ar plasma treatment, producing Ar-NiCoAl-LDHs@ACC with enlarged interlayer spacing. The carbon cloth substrate inhibited the agglomeration of NiCoAl-LDHs nanosheets and improved electrical conductivity, while Ar plasma treatment further expanded the interlayer spacing and enhanced hydrophilicity, providing fast chloride ion diffusion channels and releasing more interlayer active sites, achieving high desalination kinetics. Ar-NiCoAl-LDHs@ACC was used as the chloride removal electrode and assembled with activated carbon into a hybrid capacitive deionization (HCDI) device. In 1000 mg L−1 NaCl solution at 1.2 V, the salt removal capacity reached 93.26 mg g−1, the salt removal rate reached 0.27 mg g−1 s−1, and the charge efficiency was as high as 0.97. In 300 mg L−1 NaCl solution at 0.8 V, the capacity retention remained above 85% after 100 cycles. This work provides a new strategy for the controllable preparation of two-dimensional metal hydroxide materials with large interlayer spacing and the design of high-performance electrochemical chloride removal electrodes.
1. Introduction
The global increase in water consumption has led to high water stress both domestically and internationally, making it urgent to address the shortage of fresh water resources. Desalination is one of the effective methods to solve this problem [1,2]. Traditional thermal, membrane, and ion exchange methods suffer from high equipment costs, high energy consumption, and secondary pollution [3,4], which are not conducive to sustainable development. Capacitive deionization (CDI) has attracted attention due to its energy efficiency, economy, and environmental friendliness, emerging as a promising desalination technology [5,6]. CDI works by applying an electric field across electrodes, causing ions in the solution to migrate toward oppositely charged electrodes, thereby reducing ion concentration and achieving desalination.
Conventional CDI typically uses carbon materials such as activated carbon [7], carbon aerogels [8], carbon nanotubes [9], and graphene [10] as electrodes, which store charge via electrical double layers, offering fast desalination rates [11]. However, carbon electrodes suffer from co-ion repulsion effects, leading to low charge efficiency [12]. In contrast, Faradaic electrodes operate through ion intercalation/deintercalation, providing higher ion selectivity, charge efficiency, and salt removal capacity [12,13]. Most research has focused on sodium-removal materials (e.g., manganese oxides, titanium oxides, Prussian blue analogs), while studies on chloride-removal electrodes are relatively scarce. Current chloride removal electrodes mainly include Ag/AgCl and Bi/BiOCl [14], but these materials exhibit slow chloride removal rates and are prone to hydrogen/oxygen evolution reactions [15]. Layered double hydroxides (LDHs) have high electrochemical activity and can undergo rapid reversible redox reactions, leading to faster desalination rates. LDHs are two-dimensional layered materials with the general formula [M2+1−xM3+x(OH)2]2+[An−x/n·mH2O], where M2+ and M3+ are divalent and trivalent metal cations, and An− is an interlayer anion [16]. LDHs can store anions through interlayer intercalation, making them suitable for anion adsorption.
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Qiutong Jiang, Guoqing Wang, Yi Li, Hongwei Huang, Qian Li, Jian Yang (2024). Plasma-assisted preparation of carbon cloth-supported NiCoAl-LDHs with large interlayer spacing for electrochemical deionization. New Carbon Materials. https://doi.org/10.1016/S1872-5805_N
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Frequently Asked Questions
What is the main innovation of this study?
The study introduces a plasma-assisted method to enlarge the interlayer spacing of NiCoAl-LDHs grown on flexible carbon cloth, enhancing chloride ion diffusion and active site availability, leading to high-performance capacitive deionization.
How does the Ar plasma treatment improve the desalination performance?
Ar plasma treatment expands the interlayer spacing of NiCoAl-LDHs and improves hydrophilicity, which facilitates rapid chloride ion diffusion and exposes more active sites, thereby increasing salt removal capacity and rate.
What are the key performance metrics of the Ar-NiCoAl-LDHs@ACC electrode?
In 1000 mg L−1 NaCl at 1.2 V, the electrode achieves a salt removal capacity of 93.26 mg g−1, a rate of 0.27 mg g−1 s−1, and a charge efficiency of 0.97. It retains over 85% capacity after 100 cycles in 300 mg L−1 NaCl at 0.8 V.
Why is the carbon cloth substrate beneficial?
The carbon cloth provides a conductive and flexible support that inhibits nanosheet agglomeration, improves electrical conductivity, and allows the electrode to be used directly without binders or conductive additives, enhancing overall performance.
What is the significance of this work for desalination technology?
This work offers a new strategy for designing high-performance chloride removal electrodes with large interlayer spacing, potentially advancing energy-efficient and cost-effective desalination technologies for brackish water.
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