Sequential treatment of cyanide and phenolic mixtures using CMC-PVP-nZVI/Pd and <i>Rhodococcus pyridinivorans</i> strain PDB9T N1

Cyanide and phenol are considered the major toxic pollutants in coke-oven wastewater. Cyanide, at a pH less than 10, is converted to HCN gas (p<i>K</i> <sub>a</sub> = 9.2). Hence, cyanide treatment requires strongly alkaline conditions, <i>i.e.</i>, a pH of more than 10; however, at such a high pH, the viability of microbes is not feasible. Therefore, to overcome this incompatibility, a sequential nano-bio treatment system was developed, integrating a novel carboxymethyl cellulose-polyvinylpyrrolidone-stabilized nanoscale zero-valent iron doped with palladium (CMC-PVP-nZVI/Pd) nanocomposite, followed by bio-treatment using <i>R. pyridinivorans</i> strain PDB9T N-1. The first nanostage was operated at pH 12 to stabilize cyanide (CN<sup>-</sup>) and initiate its removal, while the subsequent biostage was operated at a pH of 7.4 to achieve the complete removal of phenol. To prevent the atmospheric oxidation of nZVI and to improve its reusability and electron mobility, it was doped with palladium and conjugated with CMC and PVP. The synthesised nanomaterials were characterized using XRD, FTIR spectroscopy, FESEM, EDX, and XPS analyses. Results revealed that about 99% of cyanide was removed with an initial dose of 100 mg L<sup>-1</sup> at 30 °C using the nanocomposite, followed by the complete biodegradation of the remaining phenol (300 mg L<sup>-1</sup>). The cyanide removal efficiency of the nanocomposite was 1.8-fold higher than that of the bare nZVI. Overall, the cyanide removal process followed a pseudo-2nd-order kinetics model, revealing a chemisorption nature with a superior sorption capacity of 93.37 mg g<sup>-1</sup>. The intraparticle diffusion model showed that exterior mass transfer primarily governed the cyanide removal. Additionally, the nanocomposite exhibited strong reusability, demonstrating the efficacy of the proposed sequential nano-bio system.

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Publication Details

Journal
Nanoscale Advances
Published
2025-12-19
DOI
https://doi.org/10.1039/d5na00920k
Citations
1
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
Field-Weighted Citation Impact
0.67
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article

Sequential treatment of cyanide and phenolic mixtures using CMC-PVP-nZVI/Pd and Rhodococcus pyridinivorans strain PDB9T N1

1 citations
Nanoscale Advances
Thermochemical Biomass Conversion Processes
0.67
article

Sequential treatment of cyanide and phenolic mixtures using CMC-PVP-nZVI/Pd and Rhodococcus pyridinivorans strain PDB9T N1

article en
1 citations

Abstract

Cyanide and phenol are considered the major toxic pollutants in coke-oven wastewater. Cyanide, at a pH less than 10, is converted to HCN gas (p<i>K</i> <sub>a</sub> = 9.2). Hence, cyanide treatment requires strongly alkaline conditions, <i>i.e.</i>, a pH of more than 10; however, at such a high pH, the viability of microbes is not feasible. Therefore, to overcome this incompatibility, a sequential nano-bio treatment system was developed, integrating a novel carboxymethyl cellulose-polyvinylpyrrolidone-stabilized nanoscale zero-valent iron doped with palladium (CMC-PVP-nZVI/Pd) nanocomposite, followed by bio-treatment using <i>R. pyridinivorans</i> strain PDB9T N-1. The first nanostage was operated at pH 12 to stabilize cyanide (CN<sup>-</sup>) and initiate its removal, while the subsequent biostage was operated at a pH of 7.4 to achieve the complete removal of phenol. To prevent the atmospheric oxidation of nZVI and to improve its reusability and electron mobility, it was doped with palladium and conjugated with CMC and PVP. The synthesised nanomaterials were characterized using XRD, FTIR spectroscopy, FESEM, EDX, and XPS analyses. Results revealed that about 99% of cyanide was removed with an initial dose of 100 mg L<sup>-1</sup> at 30 °C using the nanocomposite, followed by the complete biodegradation of the remaining phenol (300 mg L<sup>-1</sup>). The cyanide removal efficiency of the nanocomposite was 1.8-fold higher than that of the bare nZVI. Overall, the cyanide removal process followed a pseudo-2nd-order kinetics model, revealing a chemisorption nature with a superior sorption capacity of 93.37 mg g<sup>-1</sup>. The intraparticle diffusion model showed that exterior mass transfer primarily governed the cyanide removal. Additionally, the nanocomposite exhibited strong reusability, demonstrating the efficacy of the proposed sequential nano-bio system.

Nanoscale AdvancesVol. 8(3)
Government of Maharashtra (IN), Siksha O Anusandhan University (IN), Institute of Minerals and Materials Technology (IN), National Institute of Hydrology (IN), Dr. B. R. Ambedkar National Institute of Technology Jalandhar (IN)
Clean water and sanitation
Openalex Percentile: Top 23%
Thermochemical Biomass Conversion Processes
0.67
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