The Chinese Journal of Process Engineering ›› 2021, Vol. 21 ›› Issue (7): 807-816.DOI: 10.12034/j.issn.1009-606X.220217
• Reaction & Separation • Previous Articles Next Articles
LI Ling1(), Lei DING1,2(
), Gang XUE1, Yunhan JIA1, Meiying ZHONG1,2, Dewei ZHANG2,3
Received:
2020-07-09
Revised:
2020-09-04
Online:
2021-07-28
Published:
2021-07-27
Contact:
Lei DING 17375087687@163.com;dinglei1978@163.com
李凌1(), 丁磊1,2(
), 薛岗1, 贾韫翰1, 钟梅英1,2, 张德伟2,3
通讯作者:
丁磊 17375087687@163.com;dinglei1978@163.com
作者简介:
李凌(1997-),男,安徽省合肥市人,硕士研究生,建筑与土木工程专业,E-mail: 17375087687@163.com基金资助:
CLC Number:
LI Ling, Lei DING, Gang XUE, Yunhan JIA, Meiying ZHONG, Dewei ZHANG. Effects of hydrophilicity/hydrophobicity of humic acid components on the removal of bromide adsorbed on magnetic ion exchange resin[J]. The Chinese Journal of Process Engineering, 2021, 21(7): 807-816.
李凌, 丁磊, 薛岗, 贾韫翰, 钟梅英, 张德伟. 不同亲疏水性腐殖酸对磁性离子交换树脂吸附去除水中溴离子的影响[J]. 过程工程学报, 2021, 21(7): 807-816.
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URL: https://www.jproeng.com/EN/10.12034/j.issn.1009-606X.220217
Parameter | MIEX |
---|---|
Type | Macroporous |
Structure | Polyacrylic |
Zero charge point/MW | 6.4 |
Particle size/mm | 0.15 |
Water content/% | 65~67.1 |
Magnetic material content/% | 8.52 |
Total pore volume/(cm3/mL) | 0.018 |
Exchange capacity/(meq/mL) | 0.32~0.65 |
BET specific surface area/(m2/g) | 21.47 |
Table 1 Performance parameters of MIEX resin[22]
Parameter | MIEX |
---|---|
Type | Macroporous |
Structure | Polyacrylic |
Zero charge point/MW | 6.4 |
Particle size/mm | 0.15 |
Water content/% | 65~67.1 |
Magnetic material content/% | 8.52 |
Total pore volume/(cm3/mL) | 0.018 |
Exchange capacity/(meq/mL) | 0.32~0.65 |
BET specific surface area/(m2/g) | 21.47 |
Zeta potential/mV | Component of HA | |||
---|---|---|---|---|
VHC | SHC | PHC | NHC | |
pH=7.0 | -12.70 | -12.60 | -9.54 | -8.78 |
Table 2 The Zeta potentials of four HA components
Zeta potential/mV | Component of HA | |||
---|---|---|---|---|
VHC | SHC | PHC | NHC | |
pH=7.0 | -12.70 | -12.60 | -9.54 | -8.78 |
Component of bromide solution | Pseudo-first order kinetic model | Pseudo-second order kinetic model | ||||||
---|---|---|---|---|---|---|---|---|
qe/ (mg/L) | k1/min-1 | R2 | SE | qe/ (mg/L) | k2/min-1 | R2 | SE | |
Br- | 0.34 | 0.170 | 0.94 | 0.008 | 0.37 | 0.710 | 0.99 | 0.005 |
Br-+HA (VHC) | 0.05 | 0.294 | 0.95 | 0.001 | 0.05 | 10.056 | 0.98 | 0.001 |
Br-+HA (SHC) | 0.03 | 0.135 | 0.91 | 0.001 | 0.03 | 6.158 | 0.96 | 0.001 |
Br-+HA (PHC) | 0.07 | 0.292 | 0.94 | 0.002 | 0.07 | 7.150 | 0.97 | 0.002 |
Br-+HA (NHC) | 0.09 | 0.229 | 0.94 | 0.003 | 0.10 | 3.761 | 0.98 | 0.003 |
Table 3 Parameters calculated from adsorption kinetics model
Component of bromide solution | Pseudo-first order kinetic model | Pseudo-second order kinetic model | ||||||
---|---|---|---|---|---|---|---|---|
qe/ (mg/L) | k1/min-1 | R2 | SE | qe/ (mg/L) | k2/min-1 | R2 | SE | |
Br- | 0.34 | 0.170 | 0.94 | 0.008 | 0.37 | 0.710 | 0.99 | 0.005 |
Br-+HA (VHC) | 0.05 | 0.294 | 0.95 | 0.001 | 0.05 | 10.056 | 0.98 | 0.001 |
Br-+HA (SHC) | 0.03 | 0.135 | 0.91 | 0.001 | 0.03 | 6.158 | 0.96 | 0.001 |
Br-+HA (PHC) | 0.07 | 0.292 | 0.94 | 0.002 | 0.07 | 7.150 | 0.97 | 0.002 |
Br-+HA (NHC) | 0.09 | 0.229 | 0.94 | 0.003 | 0.10 | 3.761 | 0.98 | 0.003 |
Component of bromide solution | Langmuir | Freundlich | ||||||
---|---|---|---|---|---|---|---|---|
qmax/(mg/mL) | kl/(L/mg) | R2 | SE | kf | 1/n | R2 | SE | |
Br- | 13.10 | 0.001 | 0.99 | 0.307 | 2.50 | 0.853 | 0.99 | 0.020 |
Br-+HA (VHC) | 1.04 | 0.304 | 0.96 | 0.630 | 0.27 | 1.046 | 0.95 | 0.186 |
Br-+HA (SHC) | 1.10 | 0.578 | 0.93 | 0.906 | 0.47 | 1.101 | 0.92 | 0.259 |
Br-+HA (PHC) | 1.73 | 0.052 | 0.95 | 0.582 | 0.91 | 0.968 | 0.95 | 0.171 |
Br-+HA (NHC) | 1.40 | 0.913 | 0.98 | 0.517 | 0.78 | 1.237 | 0.97 | 0.152 |
Table 4 Parameters calculated from adsorption equilibrium model
Component of bromide solution | Langmuir | Freundlich | ||||||
---|---|---|---|---|---|---|---|---|
qmax/(mg/mL) | kl/(L/mg) | R2 | SE | kf | 1/n | R2 | SE | |
Br- | 13.10 | 0.001 | 0.99 | 0.307 | 2.50 | 0.853 | 0.99 | 0.020 |
Br-+HA (VHC) | 1.04 | 0.304 | 0.96 | 0.630 | 0.27 | 1.046 | 0.95 | 0.186 |
Br-+HA (SHC) | 1.10 | 0.578 | 0.93 | 0.906 | 0.47 | 1.101 | 0.92 | 0.259 |
Br-+HA (PHC) | 1.73 | 0.052 | 0.95 | 0.582 | 0.91 | 0.968 | 0.95 | 0.171 |
Br-+HA (NHC) | 1.40 | 0.913 | 0.98 | 0.517 | 0.78 | 1.237 | 0.97 | 0.152 |
Component | T/K | KD/(L/mL) | ΔG0/ (kJ/mol) | ΔH0/ (kJ/mol) | ΔS0/(J/mol) |
---|---|---|---|---|---|
Br- | 288 | 18.37 | -6.77 | -92.40 | -279.33 |
293 | 7.35 | -5.28 | |||
298 | 5.05 | -3.79 | |||
Br-+VHC | 288 | 0.63 | 1.10 | 18.45 | 60.24 |
293 | 0.74 | 0.80 | |||
298 | 0.81 | 0.50 | |||
Br-+SHC | 288 | 1.23 | -0.56 | 2.16 | 9.44 |
293 | 1.37 | -0.61 | |||
298 | 1.26 | -0.65 | |||
Br-+PHC | 288 | 3.04 | -2.83 | -20.23 | -60.40 |
293 | 3.27 | -2.53 | |||
298 | 2.29 | -2.23 | |||
Br-+NHC | 288 | 2.89 | -2.70 | -21.89 | -66.61 |
293 | 3.00 | -2.37 | |||
298 | 2.12 | -2.04 |
Table 5 Thermodynamic parameters of Br- absorbed on MIEX resin in the presence of HA component
Component | T/K | KD/(L/mL) | ΔG0/ (kJ/mol) | ΔH0/ (kJ/mol) | ΔS0/(J/mol) |
---|---|---|---|---|---|
Br- | 288 | 18.37 | -6.77 | -92.40 | -279.33 |
293 | 7.35 | -5.28 | |||
298 | 5.05 | -3.79 | |||
Br-+VHC | 288 | 0.63 | 1.10 | 18.45 | 60.24 |
293 | 0.74 | 0.80 | |||
298 | 0.81 | 0.50 | |||
Br-+SHC | 288 | 1.23 | -0.56 | 2.16 | 9.44 |
293 | 1.37 | -0.61 | |||
298 | 1.26 | -0.65 | |||
Br-+PHC | 288 | 3.04 | -2.83 | -20.23 | -60.40 |
293 | 3.27 | -2.53 | |||
298 | 2.29 | -2.23 | |||
Br-+NHC | 288 | 2.89 | -2.70 | -21.89 | -66.61 |
293 | 3.00 | -2.37 | |||
298 | 2.12 | -2.04 |
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