CIESC Journal ›› 2024, Vol. 75 ›› Issue (6): 2283-2298.DOI: 10.11949/0438-1157.20240134
• Separation engineering • Previous Articles Next Articles
Yan WANG1(), Jiawen ZHOU1, Peiliang SUN2, Yong CHEN1(
), Yuanhong QI3, Chong PENG2(
)
Received:
2024-01-29
Revised:
2024-04-11
Online:
2024-07-03
Published:
2024-06-25
Contact:
Yong CHEN, Chong PENG
王岩1(), 周佳文1, 孙培亮2, 陈勇1(
), 齐元红3, 彭冲2(
)
通讯作者:
陈勇,彭冲
作者简介:
王岩(1998—),女,硕士研究生,wangyan040321@163.com
基金资助:
CLC Number:
Yan WANG, Jiawen ZHOU, Peiliang SUN, Yong CHEN, Yuanhong QI, Chong PENG. Removal of Hg2+ from water by magnetic polyaminothiazole adsorbent[J]. CIESC Journal, 2024, 75(6): 2283-2298.
王岩, 周佳文, 孙培亮, 陈勇, 齐元红, 彭冲. 磁性聚氨基噻唑吸附剂脱除水体Hg2+性能[J]. 化工学报, 2024, 75(6): 2283-2298.
Fig.2 The Hg2+ equilibrium adsorption capacity of Fe3O4@SiO2 @PAT, Fe3O4@SiO2@PDA-PAT, PAT (experimental conditions: 100 ml of wastewater with pH of 1.3 and Hg2+ concentration of 50 mg/L was absorbed by 20 mg adsorbent at 303 K for 24 h)
元素 | 峰值/eV | 元素含量/% |
---|---|---|
Hg 4f | 103.18 | — |
N 1s | 399.71 | 5.52 |
S 2p | 163.91 | 1.25 |
C 1s | 284.6 | 92.33 |
Cu 2p | 932.73 | 0.53 |
Table 1 Fe3O4@SiO2@PDA-PAT XPS elements content
元素 | 峰值/eV | 元素含量/% |
---|---|---|
Hg 4f | 103.18 | — |
N 1s | 399.71 | 5.52 |
S 2p | 163.91 | 1.25 |
C 1s | 284.6 | 92.33 |
Cu 2p | 932.73 | 0.53 |
Fig.8 Effect of adsorption time and pH on Hg2+ adsorption by Fe3O4@SiO2@PDA-PAT (experimental conditions: 100 ml of wastewater with pH of 1.3 and Hg2+ concentration of 50 mg/L was absorbed by 20 mg adsorbent at 303 K for 24 h)
Fig.9 Effect of temperature and Hg2+ concentration on the adsorption properties of Fe3O4@SiO2@PDA-PAT (experimental conditions: 100 ml wastewater with pH of 1.3 or pH of 5.0 and Hg2+ concentration of 50 mg/L was adsorbed by 20 mg adsorbent at 303 K for 24 h)
Fig.10 Relationship between mercury adsorption time and adsorption capacity of Fe3O4@SiO2@PDA-PAT at different pH (experimental conditions: 100 ml of wastewater with pH 1.3 or pH 5.0 and Hg2+ concentration of 50 mg/L, 20 mg of adsorbent)
pH | T/K | 准一级吸附动力学 | 准二级吸附动力学 | 内扩散吸附动力学 | ||||||
---|---|---|---|---|---|---|---|---|---|---|
Qe/(mg/g) | k1/min-1 | R2 | Qe/(mg/g) | k2/(g/(mg·min)) | R2 | kin | C | R2 | ||
1.3 | 297 | 98.99 | 0.0105 | 0.9602 | 119.8 | 6.26×10-5 | 0.9893 | 5.469 | -10.03 | 0.9789 |
303 | 84.95 | 0.0089 | 0.9513 | 135.9 | 1.29×10-4 | 0.9845 | 5.632 | 20.21 | 0.9744 | |
309 | 109.2 | 0.0051 | 0.9686 | 138.5 | 2.17×10-4 | 0.9987 | 7.253 | 24.20 | 0.9052 | |
5.0 | 297 | 56.42 | 0.0060 | 0.9553 | 86.43 | 1.59×10-4 | 0.9948 | 3.591 | 9.681 | 0.9007 |
303 | 134.8 | 0.0065 | 0.9539 | 179.5 | 7.97×10-5 | 0.9975 | 8.383 | -8.289 | 0.9684 | |
309 | 122.6 | 0.0048 | 0.9502 | 204.5 | 3.12×10-5 | 0.9929 | 7.253 | 24.20 | 0.9052 |
Table 2 Kinetic parameters of adsorption of Hg2+ by Fe3O4@SiO2@PDA-PAT
pH | T/K | 准一级吸附动力学 | 准二级吸附动力学 | 内扩散吸附动力学 | ||||||
---|---|---|---|---|---|---|---|---|---|---|
Qe/(mg/g) | k1/min-1 | R2 | Qe/(mg/g) | k2/(g/(mg·min)) | R2 | kin | C | R2 | ||
1.3 | 297 | 98.99 | 0.0105 | 0.9602 | 119.8 | 6.26×10-5 | 0.9893 | 5.469 | -10.03 | 0.9789 |
303 | 84.95 | 0.0089 | 0.9513 | 135.9 | 1.29×10-4 | 0.9845 | 5.632 | 20.21 | 0.9744 | |
309 | 109.2 | 0.0051 | 0.9686 | 138.5 | 2.17×10-4 | 0.9987 | 7.253 | 24.20 | 0.9052 | |
5.0 | 297 | 56.42 | 0.0060 | 0.9553 | 86.43 | 1.59×10-4 | 0.9948 | 3.591 | 9.681 | 0.9007 |
303 | 134.8 | 0.0065 | 0.9539 | 179.5 | 7.97×10-5 | 0.9975 | 8.383 | -8.289 | 0.9684 | |
309 | 122.6 | 0.0048 | 0.9502 | 204.5 | 3.12×10-5 | 0.9929 | 7.253 | 24.20 | 0.9052 |
Fig.12 The relationship between the initial Hg2+ concentration of Fe3O4@SiO2@PDA-PAT and the equilibrium adsorption capacity at pH 1.3 and 5.0 (experimental conditions: 100 ml of wastewater with pH 1.3 or pH 5.0 was absorbed by 20 mg adsorbent for 24 h)
pH | T/K | Langmuir等温吸附模型 | Freundlich等温吸附模型 | ||||
---|---|---|---|---|---|---|---|
Qm/(mg/g) | KL/(L/mg) | R2 | 1/n | KF/(mg/g) | R2 | ||
1.3 | 297 | 92.42 | 0.7723 | 0.9989 | 0.2233 | 44.95 | 0.7599 |
303 | 131.9 | 0.4446 | 0.9999 | 0.4246 | 35.22 | 0.7760 | |
309 | 159.7 | 0.3110 | 0.9996 | 0.3951 | 45.54 | 0.9426 | |
5.0 | 297 | 83.26 | 0.3099 | 0.9825 | 0.2487 | 33.01 | 0.9528 |
303 | 163.1 | 0.5104 | 0.9926 | 0.3120 | 62.69 | 0.8851 | |
309 | 176.7 | 1.018 | 0.9884 | 0.2899 | 73.89 | 0.9658 |
Table 3 Fe3O4@SiO2@PDA-PAT isotherm adsorption model for Hg2+ adsorption
pH | T/K | Langmuir等温吸附模型 | Freundlich等温吸附模型 | ||||
---|---|---|---|---|---|---|---|
Qm/(mg/g) | KL/(L/mg) | R2 | 1/n | KF/(mg/g) | R2 | ||
1.3 | 297 | 92.42 | 0.7723 | 0.9989 | 0.2233 | 44.95 | 0.7599 |
303 | 131.9 | 0.4446 | 0.9999 | 0.4246 | 35.22 | 0.7760 | |
309 | 159.7 | 0.3110 | 0.9996 | 0.3951 | 45.54 | 0.9426 | |
5.0 | 297 | 83.26 | 0.3099 | 0.9825 | 0.2487 | 33.01 | 0.9528 |
303 | 163.1 | 0.5104 | 0.9926 | 0.3120 | 62.69 | 0.8851 | |
309 | 176.7 | 1.018 | 0.9884 | 0.2899 | 73.89 | 0.9658 |
pH | T/K | R2 | ΔH/(kJ/mol) | ΔS/(J/(mol·K)) | ΔG/(kJ/mol) |
---|---|---|---|---|---|
1.3 | 297 | 0.9876 | -57.91 | -95.89 | -29.51 |
303 | -28.71 | ||||
309 | -28.36 | ||||
5.0 | 297 | 0.9892 | 75.52 | 345.8 | -27.25 |
303 | -29.06 | ||||
309 | -31.41 |
Table 4 Thermodynamic parameters of adsorption of Hg2+ by Fe3O4@SiO2@PDA-PAT
pH | T/K | R2 | ΔH/(kJ/mol) | ΔS/(J/(mol·K)) | ΔG/(kJ/mol) |
---|---|---|---|---|---|
1.3 | 297 | 0.9876 | -57.91 | -95.89 | -29.51 |
303 | -28.71 | ||||
309 | -28.36 | ||||
5.0 | 297 | 0.9892 | 75.52 | 345.8 | -27.25 |
303 | -29.06 | ||||
309 | -31.41 |
Fig.16 Effect of common metal cations (a) and Na+ (b) on the adsorption of mercury ions by Fe3O4@SiO2@PDA-PAT(experimental conditions: 100 ml of simulated wastewater with pH 1.3, Hg2+ at 20 mg/L and 400 mg/L, 20 mg adsorbent at 303 K for 24 h)
Fig.17 Desorption efficiency of Fe3O4@SiO2@PDA-PAT(experimental conditions: the adsorbent after 20 mg saturation adsorption was added into 50 ml desorption solution and desorbed at 303 K for 24 h)
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