Journal of Textile Research ›› 2025, Vol. 46 ›› Issue (01): 138-147.doi: 10.13475/j.fzxb.20240104701

• Dyeing and Finishing Engineering • Previous Articles     Next Articles

Degradation of reactive dye wastewater by titanium carbide and Fe3+ activated sodium persulfate

LI Wanxin1, SHU Dawu1,2(), AN Fangfang1, HAN Bo1, REN Zhigang2, SHAN Juchuan1   

  1. 1. College of Textile and Garments, Hebei University of Science and Technology, Shijiazhuang, Hebei 050018, China
    2. Zibo Molinhui New Material Co., Ltd., Zibo, Shandong 255000, China
  • Received:2024-01-29 Revised:2024-09-18 Online:2025-01-15 Published:2025-01-15
  • Contact: SHU Dawu E-mail:shudawu@126.com

Abstract:

Objective In order to enhance the efficiency of dyeing wastewater treatment and decrease the presence of transition metals in the process, Ti3C2 MXene was employed to reduce trace Fe3+ for rapid activation degradation of C.I. Reactive Black 5 (RB5) wastewater by sodium persulfate (SPS).

Method The RB5 solution was used as the research subject, and the degradation rate was employed as the evaluation criterion. The relationship between the concentrations of sodium persulfate (SPS), FeCl3, and MXene, initial pH was investigated, and the influence of MXene on the degradation of RB5. The contribution rate of free radicals in the process of dye degradation was investigated through free radical quenching experiments.

Results The results showed that the degradation rate of RB5 simulated wastewater was up to 99.3% when a mixture of 2.0 g/L SPS, 0.06 mmol/L FeCl3, and 60 mg/L MXene was stirred at 25 ℃ for 30 min. After MXene was applied, particle structures adhered to the surface. Furthermore, the formation of numerous Ti—O bonds and the reduction of Ti element introduced Fe element, leading to a 1.13% decrease in the crystallinity of the characteristic peak. The Fe3+/SPS/MXene system effectively degraded RB5. This is mainly attributed to MXene's role in promoting the reduction of Fe3+ to Fe2+, thereby accelerating the activation of SPS. RB5 degradation followed quasi-first-order reaction kinetics. Both Fe3+ and MXene demonstrated significant effects on the activation of SPS. The degradation efficiency of organic pollutants was modulated by changing the concentrations of Fe3+ and MXene. The degradation rate of RB5 was decreased as the pH value increased. Under alkaline conditions, iron ions were transformed into precipitates and lost their catalytic ability. This, in turn, hindered the effective degradation of dye molecules. In addition, MXene effectively prevented the hydrolysis of Fe3+ ions in water through its interlayer confinement effect. After the utilization of Ti3C2 MXene, the elemental O content was increased from 22.37% to 49.71%, suggesting that Ti3C2 MXene underwent oxidation. MXene before and after use revealed the presence of interfacial reactions between Fe3+ and MXene, resulting in the reduction of Fe3+ to Fe2+ by MXene. The degradation rate of RB5 in the Fe3+/SPS/MXene system for 30 min was 2.49% higher than that in the Fe3+/SPS/hydroxylamine process, indicating that MXene can continuously reduce Fe3+ under these conditions. When reactive dyes were degraded by the Fe3+/SPS/MXene system, the ·OH played a major role. Inorganic salts significantly altered the decolorization rate of the dye solution, but have little impact on the final decolorization rate.

Conclusion For 0.05 g/L of RB5 simulated wastewater, the optimal degradation conditions were found to be 2.0 g/L SPS, 0.06 mmol/L FeCl3, and 60 mg/L MXene. Under these conditions, the degradation rate reached as high as 99.3% after being treated at 25 ℃ for 30 min. During the degradation process, while inorganic salts like NaCl significantly altered the decolorization rate of the dye solution, but had little impact on the final decolorization rate. The strong reducing MXene not only inhibited the hydrolysis of iron ions, but also continuously reduced Fe3+ to Fe2+. When the Fe3+/SPS/MXene system was adopted to degrade RB5 simulated wastewater. Neutral pH conditions could be achieved for degrading the wastewater, with ·OH playing a major role in degradation process.

Key words: reactive dye, MXene, sodium persulfate, free radical, dye wastewater, degradation rate

CLC Number: 

  • X791

Fig.1

SEM images of MXene before (a) and after (b) use"

Fig.2

EDS (a) and XRD (b) patterns of MXene before and after use"

Fig.3

Degradation rates of RB5 in different reaction systems"

Tab.1

Quasi-first-order kinetic fitting equations and parameters for factors affecting RB5 degradation rates"

影响因素 变量 动力学方程 k/min-1 R2
SPS质量
浓度/
(g·L-1)
0 y=0.001 1x+0.009 6 0.001 1 0.97
0.5 y=0.095 4x+0.009 6 0.095 4 0.98
1.0 y=0.100 6x+0.403 7 0.100 6 0.97
2.0 y=0.150 2x+0.554 2 0.150 2 0.99
3.0 y=0.115 3x+0.682 3 0.115 3 0.98
FeCl3浓度/
(mmol·L-1)
0 y=0.000 2x+0.046 4 0.000 2 0.98
0.06 y=0.217 7x+0.794 2 0.217 7 0.95
0.12 y=0.312 1x+1.050 8 0.312 1 0.96
0.18 y=0.237 4x+1.528 8 0.237 4 0.91
0.24 y=0.260 2x+1.652 6 0.260 2 0.91
MXene质量
浓度/
(mg·L-1)
0 y=0.000 8x+0.020 5 0.000 8 0.97
30 y=0.100 7x+0.405 2 0.100 7 0.98
60 y=0.159 1x+0.409 3 0.159 1 0.99
90 y=0.161 4x+0.526 7 0.161 4 0.98
120 y=0.444 6x+0.071 7 0.444 6 0.99
pH值 3 y=0.299 5x+0.511 7 0.299 5 0.98
5 y=0.214 2x+0.529 1 0.214 2 0.96
7 y=0.180 6x+0.401 1 0.180 6 0.98
10 y=0.010 5x-0.002 5 0.010 5 0.97

Fig.4

Degradation rates of RB5 under different conditions. (a) SPS mass concentration; (b) FeCl3 concentration; (c) MXene mass concentration; (d) pH value"

Fig.5

Effect of MXene on inhibition of hydrolysis and reduction of Fe3+. (a) UV-Vis absorption spectra curves of Fe2+ in different systems; (b) UV-Vis spectra curves of Fe3+/MXene at different time periods; (c) Degradation rates of RB5 in different systems"

Tab.2

Elements composition of MXene before and after use"

使用前后 原子百分比/%
Ti O C Fe
使用前 16.46 22.37 61.16 0.00
使用后 16.45 49.71 30.34 3.50

Fig.6

XPS spectra of MXene before and after use. (a) Full spectrum of MXene XPS after use; (b) Spectra of Ti2p before use; (c) Spectra of Ti2p after use; (d) Spectra of Fe2p after use; (e) Spectra of O1s before use; (f) Spectra of O1s after use"

Fig.7

Comparison of MXene reduction performance. (a) Influence of Fe3+ molar concentration on absorbance; (b) Comparison of reduction performance of MXene and hydroxylamine"

Fig.8

Relationship between free radical type and RB5 degradation rate"

Tab.3

Quasi-first-order kinetic degradation rate of RB5 in presence of methanol and TBA"

猝灭剂 k/min-1 活性物质 贡献率/%
0.152 ·OH+S O 4 · -+其它 100.00
甲醇 0.002 其它 1.32
叔丁醇 0.004 S O 4 · -+其它 2.63

Fig.9

Relationship between degradation rate of dyeing wastewater and time"

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