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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

Postal Subscription Code 80-969

2018 Impact Factor: 2.809

Front. Chem. Sci. Eng.    2024, Vol. 18 Issue (2) : 21    https://doi.org/10.1007/s11705-024-2386-4
Recyclable hydrolyzed polymers of intrinsic microporosity-1/Fe3O4 magnetic composites as adsorbents for selective cationic dye adsorption
Feng Zhang, Shuainan Xu, Xiumei Geng, Meixia Shan(), Yatao Zhang()
School of Chemical Engineering, Zhengzhou University, Zhengzhou 450001, China
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Abstract

Polymers of intrinsic microporosity shows great potential for dye adsorption and magnetic Fe3O4 are easy to be separated. In this work, hydrolyzed polymers of intrinsic microporosity-1/Fe3O4 composite adsorbents were prepared by phase inversion and hydrolysis process for cationic dye adsorption. The chemical structure and morphology of the composite adsorbents were systematically characterized by several characterization methods. Using methylene blue as the target dye, the influences of solution pH, contact time, initial dye concentration, and system temperature on the methylene blue adsorption process were investigated. The incorporation of Fe3O4 particle into hydrolyzed polymers of intrinsic microporosity-1 endow the adsorbent with high magnetic saturation (20.7 emu·g–1) which allows the rapid separation of the adsorbent. Furthermore, the adsorption process was simulated by adsorption kinetics, isotherms and thermodynamics to gain insight onto the intrinsic adsorption mechanism. In addition, the composite adsorbents are able to selectively adsorb cationic dyes from mixed dyes solution. Hydrolyzed polymers of intrinsic microporosity/Fe3O4 shows only a slight decrease for methylene blue adsorption after 10 adsorption/regeneration cycles, demonstrating the outstanding regeneration performance. The high adsorption capacity, outstanding regeneration ability, together with simple preparation method, endow the composite adsorbents great potential for selective removal of cationic dyes in wastewater system.

Keywords polymers of intrinsic microporosity      magnetic adsorbent      cationic dye adsorption     
Corresponding Author(s): Meixia Shan,Yatao Zhang   
Just Accepted Date: 01 December 2023   Issue Date: 16 January 2024
 Cite this article:   
Feng Zhang,Shuainan Xu,Xiumei Geng, et al. Recyclable hydrolyzed polymers of intrinsic microporosity-1/Fe3O4 magnetic composites as adsorbents for selective cationic dye adsorption[J]. Front. Chem. Sci. Eng., 2024, 18(2): 21.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-024-2386-4
https://academic.hep.com.cn/fcse/EN/Y2024/V18/I2/21
Fig.1  Digital photo of the preparation methodology and magnetism separation of HPIM/Fe3O4.
Fig.2  (a) Schematic of the preparation procedure of HPIM-1; (b) XRD patterns of PIM-1, Fe3O4, and HPIM/Fe3O4; (c) 1H NMR (nuclear magnetic resonance) spectra of PIM-1 and HPIM-1; (d) FTIR spectra of PIM-1 and HPIM-1/Fe3O4 (before and after adsorption); (e) XPS spectra of PIM-1 and HPIM-1/Fe3O4 (before and after adsorption); (f) magnetization curves of Fe3O4 and HPIM/Fe3O4; (g) N2 adsorption/desorption isotherms of HPIM-1, PIM-1, and HPIM/Fe3O4 (insert: pore width distribution of HPIM/Fe3O4).
Fig.3  SEM images of (a) Fe3O4 and (b) HPIM/Fe3O4, (c) TEM image and elemental maps of HPIM/Fe3O4.
Fig.4  (a) Comparison of MB adsorption capacity among Fe3O4, PIM-1, HPIM-1, and HPIM/Fe3O4 under the following conditions: adsorbent dose: 10 mg, MB concentration: 100 mg·L–1, contact time: 5 h, T = 25 °C. (b) Comparison of the effect of pH on the adsorption capacity of HPIM/Fe3O4 under the following conditions: adsorbent dose: 10 mg, MB concentration: 100 mg·L–1, contact time: 5 h, T = 25 °C. (c) Evaluation of the zeta potential of HPIM/Fe3O4 at different pH values under the following conditions: adsorbent dose: 10 mg, MB concentration: 100 mg·L–1, contact time: 5 h, T = 25 °C. (d) Ionic strength (C0 = 100 mg·L–1) on the adsorption capacity of HPIM/Fe3O4 toward MB at 25 °C.
Fig.5  (a) Influence of contact time on the adsorption capacity of HPIM/Fe3O4 (adsorbent dose: 10 mg; MB concentration: 100 mg·L–1, contact time: 20–480 min, T = 25 °C, pH = 9); (b) PSO model; (c) intraparticle diffusion model fitted curves of MB adsorption on HPIM/Fe3O4; (d) influence of initial concentration on the adsorption capacity of HPIM/Fe3O4 (adsorbent dose: 10 mg, MB concentration: 50–500 mg·L–1, contact time: 5 h, T = 25 °C, pH = 9); (e) the Langmuir model and (f) the plot of lnKc vs. 1/T for thermodynamic assessment of MB adsorption on HPIM/Fe3O4.
C0/(mg·L–1)PFOPSO
K1/min–1qe/(mg·g–1)R2K2/(103·g·mg–1·min–1)qe/(mg·g–1)R2
1000.0154136.10.9690.217207.90.999
2000.0113158.90.9000.118306.80.999
Tab.1  Kinetic parameters of PFO and PSO model for MB adsorption by HPIM/Fe3O4
C0 /(mg·L–1)k1k2k3C1C2C3R12R22R32
(mg·g–1·min–1/2
10010.646.370.2869.5598.99191.060.9990.9930.930
20019.5511.770.9660.76111.84266.680.9950.9820.447
Tab.2  Kinetic parameters of intraparticle diffusion model for MB adsorption by HPIM/Fe3O4
KL/(L·mg–1)Langmuir modelFreundlich model
qm/(mg·g–1)RLR2KFnR2
0.0110413.20.64–0.150.98138.196.080.90
Tab.3  Isotherm parameters for MB adsorption by HPIM/Fe3O4
T/Kqe/(mg·g–1)ΔG/(kJ·mol–1)ΔH/(kJ·mol–1)ΔS/(J·K–1·mol–1)R2
278.15132.4–3.102.0880.40.98
288.15147.4–4.06
298.15157.4–4.87
308.15162.5–5.44
318.15167.7–6.09
Tab.4  Thermodynamic parameters for MB adsorption by HPIM/Fe3O4
Fig.6  (a) Influence of temperature on the adsorption capacity of HPIM/Fe3O4 (adsorbent dose: 10 mg, MB concentration: 100 mg·L–1, contact time: 5 h, T = 5–45 °C). (b) Recycling adsorption capacity results of HPIM/Fe3O4 (adsorbent dose: 10 mg, MB concentration: 100 mg·L–1, contact time: 5 h, T = 25 °C).
Fig.7  UV-Vis spectra of (a) Rh-B, (b) MS, (c) MG, (d) MO, (e) CR, and (f) MO/MB before and after adsorption (adsorbent dose: 10 mg, dye concentration: 10 mg·L–1, contact time: 5 h, T = 25 °C).
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