2021
DOI: 10.1016/j.jhazmat.2020.124608
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Prussian blue analogs-based layered double hydroxides for highly efficient Cs+ removal from wastewater

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Cited by 42 publications
(12 citation statements)
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“…Specifically, due to the smaller solubility of PBA, Ni 2+ and Mn 2+ released from NiMn-LDH combined with [Fe(CN) 6 ] 3− , leading to the nucleation and subsequent growth of NiMn-PBA. 38,39 The presence of 2D host (MXene and GO) effectively restricted the aggregation of PBA crystals because of the strong electrostatic attraction. 40 Ni 0.8 Mn 0.2 -LDH nanosheets can be homogeneously dispersed in water (Figure 2a).…”
Section: ■ Results and Discussionmentioning
confidence: 99%
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“…Specifically, due to the smaller solubility of PBA, Ni 2+ and Mn 2+ released from NiMn-LDH combined with [Fe(CN) 6 ] 3− , leading to the nucleation and subsequent growth of NiMn-PBA. 38,39 The presence of 2D host (MXene and GO) effectively restricted the aggregation of PBA crystals because of the strong electrostatic attraction. 40 Ni 0.8 Mn 0.2 -LDH nanosheets can be homogeneously dispersed in water (Figure 2a).…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“…In comparison with direct transformation of bare LDH, a dramatic decrease in PBA particle size was observed on the 2D host. Specifically, due to the smaller solubility of PBA, Ni 2+ and Mn 2+ released from NiMn-LDH combined with [Fe­(CN) 6 ] 3– , leading to the nucleation and subsequent growth of NiMn-PBA. , The presence of 2D host (MXene and GO) effectively restricted the aggregation of PBA crystals because of the strong electrostatic attraction …”
Section: Resultsmentioning
confidence: 99%
“…In this study, the Thomas model is introduced to describe and predict the dynamic behavior of the Fiber-KZrTS material in the column. The model is based on Langmuir adsorption and can be written as follows c italict c 0 = 1 1 + exp [ true( k Th v true) false( m q 0 c 0 v t false) ] where k Th (L/(mg min)) is the Thomas rate constant and q 0 (mg/g) is the adsorption volume.…”
Section: Methodsmentioning
confidence: 99%
“…In the above formula, K d (L•g −1 ) is the thermodynamic distribution coefficient; T (K) is the thermodynamic temperature of the adsorption process; R (8.314 J•mol −1 •K −1 ) is the ideal gas mole constant; and ΔH (kJ•mol −1 ), ΔG (kJ•mol −1 ), and ΔS (J•mol −1 •K −1 ) are enthalpy change, Gibbs free energy, and entropy change, respectively. 28 The thermodynamic adsorption parameters of KZrTS at 298, 308, 318, and 328 K (ΔH 0 , ΔG 0 , and ΔS 0 ) can be calculated by the slope and intercept of ln K d and 1000/T curves, and the results are shown in Table 1.…”
Section: Kzrts Experimentalmentioning
confidence: 99%
“…However, the limited direct use of MHCFs made it attractive to immobilize MHCFs onto substrate materials, which severely reduced cesium adsorption capacity. erefore, a variety of approaches have been taken into account to maximize the performance of MHCFs, mainly focusing on the immobilization form or structure of composites [33][34][35][36][37]. An outstanding MHCF could also make a breakthrough in the adsorption performance of composite adsorbents.…”
Section: Introductionmentioning
confidence: 99%