Abstract

Addressing the problem of high chemical oxygen demands (COD) of cutting fluid waste generated in the machining process, its complex composition, and the specific conditions required for the treatment process, a heterogeneous Fenton fibre catalyst (NZVI@ACF) made of nanometer-iron supported on activated carbon fiber using dip-molding was developed. NZVI was homogeneously loaded onto ACF surfaces to form NZVI@ACF, with a specific surface area (SBET) of 726.3642 m2/g. Using a multistage chemical pretreatment, the NZVI@ACF/H2O2 system was used to effectively treat cutting fluid waste. The results indicated that the rate of COD removal in the cutting fluid waste liquid pretreated with NZVI@ACF/H2O2 system was 99.8% when the reactions conditions were optimized to 20 nmol/L H2O2, 6 g/L NZVI@ACF, total reaction time of 120 min and pH 5. The treated waste solution passed China’s tertiary wastewater discharge standards. NZVI@ACF/H2O2 demonstrated an excellent catalytic performance compared to the traditional Fenton catalyst, increased the effective pH reaction range and had an adsorption effect on the waste liquid after the reaction.

Highlights

  • A heterogeneous Fenton system can be used in a broader PH range than the traditional Fenton system[24,25], where iron ions remain on the surface of the heterogeneous catalyst for reuse[26,27]

  • This study was based on the heterogeneous Fenton system made from NZVI @ACF that had undergone a multi-stage chemical pretreatment to produce a NZVI@ACFS/H2O2 system

  • The efficacy of this NZVI@ACF/H2O2 system compared to the traditional flocculation-Fenton system was studied under different conditions to determine the influence of pH, amount of catalyst, H2O2 dosage and reaction time

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Summary

Introduction

A heterogeneous Fenton system can be used in a broader PH range than the traditional Fenton system[24,25], where iron ions remain on the surface of the heterogeneous catalyst for reuse[26,27]. The results indicated a 99.8% reduction in COD in the waste after treatment with the multi-stage chemical pretreated NZVI@ACFS/H2O2 system, and a greater tolerance of a broader range of pH values, compared to the traditional Fenton reaction.

Results
Conclusion
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