Journal of Textile Research ›› 2026, Vol. 47 ›› Issue (1): 54-62.doi: 10.13475/j.fzxb.20250603301

• Fiber Materials • Previous Articles     Next Articles

Preparation and Cr(Ⅵ) adsorption of polyacrylonitrile/covalent organic framework composite nanofiber membranes

LING Lei1, CHEN Kai1, GAO Jun1, WU Dingsheng1, WANG Dengbing2, ZHANG Chun3, FENG Quan1()   

  1. 1. College of Textiles and Garments, Anhui Polytechnic University, Wuhu, Anhui 241000, China
    2. School of Materials and Chemical Engineering, Wuhu University, Wuhu, Anhui 241000, China
    3. Jiangsu JIUWU HI-TECH Co., Ltd., Nanjing, Jiangsu 211800, China
  • Received:2025-06-17 Revised:2025-10-24 Online:2026-01-15 Published:2026-01-15
  • Contact: FENG Quan E-mail:fengquan@ahpu.edu.cn

Abstract:

Objective In view of the serious threat cauced by hexavalent chromium (Cr(Ⅵ)) pollution to the ecological environment and human health, current mainstream adsorbent materials still have significant limitations in terms of removal efficiency and recycling. Therefore, the development of highly efficient, stable, and highly selective adsorptive detoxification materials for the treatment of Cr(Ⅵ)-containing wastewater has important practical significance.

Method Polyacrylonitrile (PAN)/1,4-phenylenediamine (Pa) blended fibers were prepared by electrospinning, which were immersed in a solution of 1,3,5-benzenetricarboxaldehyde (Tp) to in situ grow covalent organic framework (COF), thus obtaining a composite membrane. The membrane was characterized by scanning electron microscopy (SEM), X-ray diffractometer (XRD), Fourier transform infrared spectrometer (FT-IR) and X-ray photoelectron spectrometer (XPS). Its adsorption performance was evaluated under conditions of different pH values, temperatures and Cr(Ⅵ) concentrations, and its adsorption isotherm, adsorption thermodynamics and adsorption kinetics were analyzed.

Results The surface of the raw electrospun PAN/Pa fibers was smooth and uniform. Following the in situ growth of the COF, a nanoscale dendritic COF morphology was successfully constructed on the fiber surface, forming a hierarchical porous network and significantly increasing roughness. XRD patterns showed the characteristic crystal planes of the COF, while FT-IR spectra displayed the distinct C≡N vibration of PAN and the key functional group vibrations (C=O, C—N, N—H) of the COF. The attenuation of amino-related FT-IR peaks after Cr(VI) adsorption indicated the direct participation of these groups in the adsorption process. The composite PAN/COF nanofiber membrane exhibited enhanced rigidity, with a tensile stress of 8.3 MPa, a strain of 8.8%, and an elastic modulus of 94.3 MPa, compared to the more ductile pure PAN/Pa membrane. Its hydrophilicity was also improved, evidenced by a decrease in the water contact angle from 65.18° to 49.65°. Adsorption performance for Cr(VI) was highly dependent on solution conditions; and capacity increased with temperature and decreased with rising pH. This pH dependence is attributed to the protonation of amino groups under acidic conditions, enhancing electrostatic attraction, while deprotonation occurs under alkaline conditions. A maximum adsorption capacity of 99.4 mg/g was achieved under the conditions of 318 K and pH=1. Analysis of the adsorption process revealed that the isotherm conformed to the Freundlich model, suggesting multilayer adsorption on a heterogeneous surface. Thermodynamic parameters confirmed the process was spontaneous and endothermic. Adsorption kinetics followed the pseudo-second-order model, and XPS analysis indicated that approximately 46.7% of the adsorbed Cr(VI) was reduced to less toxic Cr(III), jointly pointing to a dominant chemisorption mechanism. Furthermore, the membrane demonstrated promising reusability, maintaining over 80% of its initial adsorption efficiency after seven adsorption-desorption cycles.

Conclusion The PAN/COF composite nanofiber membrane was prepared by electrospinning and in situ growth method for the adsorption and reduction treatment of Cr(Ⅵ)-containing wastewater. Characterizations by SEM, XRD and FT-IR prove that the PAN/COF composite nanofiber membrane with good mechanical properties and hydrophilicity has been successfully prepared. The influences factors such as temperature, pH value, initial Cr(Ⅵ) concentration and contact time on the adsorption performance were studied. The results showed that at 318 K and pH=1, the maximum adsorption capacity of the membrane for 100 mg/L Cr(Ⅵ) could reach 99.4 mg/g. The study of the adsorption mechanism indicated that the adsorption process of Cr(Ⅵ) on the PAN/COF composite membrane conformed to the characteristics of multi-molecular layer adsorption, was a spontaneous endothermic reaction, and was dominated by chemical adsorption. In addition, the composite membrane has good reduction performance and reusability.

Key words: hexavalent chromium, polyacrylonitrile, covalent organic framework, electrospinning, nanofiber membrane, adsorption, wastewater treatment, heavy metal ion

CLC Number: 

  • TQ340.64

Fig.1

SEM images of nanofiber membranes"

Fig.2

XRD patterns of materials"

Fig.3

XPS total patterns (a) and FT-IR spectra (b) of materials"

Fig.4

Mechanical and hydrophilic properties of different samples. (a) Stress-strain curves; (b) Static contact angles"

Tab.1

Influence of temperature on adsorption performance of different samples"

样品名称 吸附量/(mg·g-1)
298 K 308 K 318 K
PAN/Pa 37.2 54.3 58.3
PAN/COF 52.1 76.0 99.4

Fig.5

Influence of pH value on Cr(Ⅵ) adsorption performance of PAN/COF composite nanofiber membrane"

Fig.6

Influence of Cr(Ⅵ) mass concentration on Cr(Ⅵ) adsorption performance of PAN/COF composite nanofiber membrane"

Fig.7

Adsorption isotherm. (a) Nonlinear isotherm at 298 K; (b) Nonlinear isotherm at 308 K; (c) Nonlinear isotherm at 318 K; (d) Langmuir adsorption isotherm; (e) Freundlich adsorption isotherm"

Tab.2

Adsorption isotherm parameters"

温度/K Langmuir模型 Freundlich模型
Qm/(mg·g-1) KL/(L·mg-1) R2 KF/(mg(1-n)·Ln·g-1) n R2
298 70.76 0.045 0.988 23.59 0.208 0.975
308 105.07 0.078 0.985 0.021 8 0.839 0.999
318 116.11 0.267 0.998 63.85 0.132 0.989

Fig.8

Adsorption thermodynamics. (a) Influence of temperature on Langmuir reaction rate constant; (b) Van't Hoff plot"

Tab.3

Adsorption thermodynamic parameters"

温度/K Qm/
(mg·g-1)
KL/
(L·mg-1)
ΔG/
(kJ·mol-1)
ΔH/
(kJ·mol-1)
ΔS/
(J·K-1)
298 70.76 0.045 2 7 672.19 70 347.39 209.25
308 105.07 0.077 8 6 539.07
318 116.11 0.267 4 3 487.27

Fig.9

Adsorption kinetics models. (a) Nonlinear fitting of pseudo first and pseudo second order dynamics; (b) Adsorption kinetic model of Pseudo-first-order; (c) Adsorption kinetic model of Pseudo-second-order"

Tab.4

Adsorption kinetic model parameters"

准一级 准二级
Qe=47.30 mg/g Qe=54.55 mg/g
k1=0.007 75 min-1 k2=0.017 56 g/(mg·min)
R2=0.959 R2=0.996

Fig.10

XPS spectra. (a) XPS total spectra; (b) Cr 2p fine spectra"

Fig.11

Reusable performance of PAN/COF composite nanofiber membrane"

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