Chinese Journal of Applied Chemistry ›› 2024, Vol. 41 ›› Issue (2): 297-307.DOI: 10.19894/j.issn.1000-0518.230319
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Tao ZHANG1, Si-Ying LI1, Jun-Le LI1, Si-Yu SHAO1, Chuan-Dong WU2,3, Mei LING1, Dong-Wei LYU1, Wei WANG2()
Received:
2023-10-13
Accepted:
2024-01-18
Published:
2024-02-01
Online:
2024-03-05
Contact:
Wei WANG
About author:
wangweirs@hit.edu.cnSupported by:
CLC Number:
Tao ZHANG, Si-Ying LI, Jun-Le LI, Si-Yu SHAO, Chuan-Dong WU, Mei LING, Dong-Wei LYU, Wei WANG. Performance of Granular Lanthanum Oxycarbonate in Removing Fluorine from Water[J]. Chinese Journal of Applied Chemistry, 2024, 41(2): 297-307.
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URL: http://yyhx.ciac.jl.cn/EN/10.19894/j.issn.1000-0518.230319
Kinetic model | ρ(fluoride ions)/(mg·L-1) | Formula | R2 |
---|---|---|---|
5 | y=-0.00063x+0.4763 | 0.882 5 | |
Quasi-first-order kinetic model | 10 | y=-0.00138x+1.8514 | 0.826 0 |
20 | y=-0.00058x+2.5190 | 0.990 4 | |
5 | y=0.2073x+17.1663 | 0.996 9 | |
Quasi-second-order kinetic model | 10 | y=0.0973x+18.8842 | 0.993 2 |
20 | y=0.0609x+29.2919 | 0.942 4 |
Table 1 Kinetic models for the adsorption of fluoride ions on La2O2CO3 material (25 ℃)
Kinetic model | ρ(fluoride ions)/(mg·L-1) | Formula | R2 |
---|---|---|---|
5 | y=-0.00063x+0.4763 | 0.882 5 | |
Quasi-first-order kinetic model | 10 | y=-0.00138x+1.8514 | 0.826 0 |
20 | y=-0.00058x+2.5190 | 0.990 4 | |
5 | y=0.2073x+17.1663 | 0.996 9 | |
Quasi-second-order kinetic model | 10 | y=0.0973x+18.8842 | 0.993 2 |
20 | y=0.0609x+29.2919 | 0.942 4 |
T/K | Langmuir | Freundlich | ||||
---|---|---|---|---|---|---|
qm/(mg·g-1) | b/(L·mg-1) | R2 | Kf/(mg·g-1) | n | R2 | |
298.15 | 22.47 | 2.38 | 0.991 | 13.79 | 7.13 | 0.862 |
308.15 | 24.81 | 2.87 | 0.992 | 16.62 | 7.20 | 0.780 |
313.15 | 27.64 | 3.00 | 0.997 | 18.35 | 6.84 | 0.828 |
Table 2 Fitting parameters of adsorption contour line temperature and related subjects of La2O2CO3 at different temperatures
T/K | Langmuir | Freundlich | ||||
---|---|---|---|---|---|---|
qm/(mg·g-1) | b/(L·mg-1) | R2 | Kf/(mg·g-1) | n | R2 | |
298.15 | 22.47 | 2.38 | 0.991 | 13.79 | 7.13 | 0.862 |
308.15 | 24.81 | 2.87 | 0.992 | 16.62 | 7.20 | 0.780 |
313.15 | 27.64 | 3.00 | 0.997 | 18.35 | 6.84 | 0.828 |
Fluoride removal agent | Adsorption capacity/(mg·g-1) | Ref. |
---|---|---|
Aluminum hydroxide | 18.90 | [ |
Manganese-oxide-coated alumina | 7.56 | [ |
Neodymium-modified chitosan | 22.38 | [ |
Activated alumina | 16.34 | [ |
Granular ceramic adsorption | 12.12 | [ |
Granular zirconium-iron oxide | 9.80 | [ |
Meso-structured zirconium phosphate | 4.27 | [ |
Granular lanthanum oxycarbonate | 27.64 | This study |
Lanthanum oxide | 2.50 | [ |
Lanthanum hydroxide | 11.9 | [ |
Table 3 Comparison of adsorption capacity of different fluoride removal agents
Fluoride removal agent | Adsorption capacity/(mg·g-1) | Ref. |
---|---|---|
Aluminum hydroxide | 18.90 | [ |
Manganese-oxide-coated alumina | 7.56 | [ |
Neodymium-modified chitosan | 22.38 | [ |
Activated alumina | 16.34 | [ |
Granular ceramic adsorption | 12.12 | [ |
Granular zirconium-iron oxide | 9.80 | [ |
Meso-structured zirconium phosphate | 4.27 | [ |
Granular lanthanum oxycarbonate | 27.64 | This study |
Lanthanum oxide | 2.50 | [ |
Lanthanum hydroxide | 11.9 | [ |
T/K | ΔG0/(kJ·mol-1) | ΔS0/(kJ·mol-1·K-1) | ΔH0/(kJ·mol-1) |
---|---|---|---|
298.15 | -2.155 7 | ||
308.15 | -2.705 1 | 48.299 4 | 12.229 |
313.15 | -2.862 7 |
Table 4 Thermodynamic data of La2O2CO3 adsorption of fluoride ions
T/K | ΔG0/(kJ·mol-1) | ΔS0/(kJ·mol-1·K-1) | ΔH0/(kJ·mol-1) |
---|---|---|---|
298.15 | -2.155 7 | ||
308.15 | -2.705 1 | 48.299 4 | 12.229 |
313.15 | -2.862 7 |
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