4.6 Article

Applicability of magnetic biochar derived from Fe-enriched sewage sludge for chromate removal from aqueous solution

Journal

CHEMICAL ENGINEERING SCIENCE
Volume 281, Issue -, Pages -

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ces.2023.119145

Keywords

Adsorption; Biochar; Biomass valorization; Chromate; Waste recycling

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In this study, inexpensive biochar derived from different feedstock was synthesized and tested for Cr(VI) removal from synthetic wastewater. The physical properties of the biochar were analyzed using various techniques, and the effects of different factors on Cr(VI) removal were determined. The results showed that the biochar derived from sludge had the highest Cr(VI) removal and under optimized conditions, complete removal of Cr(VI) could be achieved. The removal mechanism was based on the reduction of Cr(VI) by nZVI on the biochar. Overall, iron-enriched sewage sludge biochar is a promising and cost-effective solution for treating low-level Cr(VI)-contaminated wastewater.
In this work, inexpensive biochar derived from different feedstock was synthesized, characterized, and tested for Cr(VI) removal from synthetic wastewater. The physical properties of the sludge-based magnetic biochars (SSB) were analyzed using FT-IR, XRD, BET surface area, SEM-EDS, and XPS techniques. The effects of pyrolysis temperature (300-900 & DEG;C), initial Cr(VI) concentration (2-30 mg/L), rotation speed (50-200 rpm), pH (3-11), and co-ions (Na+, Ca2+, Mg2+, K+, Cl , HCO3  and SO42 ) on Cr(VI) removal by the SSB were determined in batch modes. It was found that the SSB had the highest Cr(VI) removal (43.7%), as compared to the other feedstock derived biochars (p & LE; 0.05; Anova test). The characterization data indicated that with an increasing pyrolysis temperature from 300 to 900 & DEG;C, the surface area, pore volume, and pore size decreased, while the Fe3O4 on SSB was gradually reduced to & alpha;-Fe0. With respect to Cr(VI) removal, under the optimized conditions of 900 & DEG;C of pyrolysis temperature, 2 mg/L of Cr(VI) concentration, 200 rpm of agitation speed, and pH 6.8, a complete Cr (VI) removal could be attained by the SSB900. Its treated effluents could comply with the required Cr(VI) discharge limit of <0.01 mg/L (GB3838-2002) mandated by local legislation. Therefore, further treatment was not required, avoiding additional cost. Coexisting ions experiments showed that all of them inhibited the Cr(VI) removal by the adsorbent after 1 h of reaction. The Cr(VI) removal followed the pseudo-second-order kinetics and the Langmuir isotherm model. The removal mechanism was based on the reduction of Cr(VI) by nZVI on the SSB900 and the Fe leakage might have facilitated the Cr(VI) removal. Overall, iron-enriched sewage sludge biochar is promising and cost-effective for treatment of low-level Cr(VI)-contaminated wastewater.

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