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Biochar is a promising sorbent for Cd removal from water, while the disposal of the exhausted Cd-enriched biochar remains a challenge. In this study, pyrolysis was employed to treat the exhausted biochar under N and CO atmospheres at 600-900 °C, and the fate of Cd during pyrolysis and characteristics of high-valued products were determined. The results indicated that higher temperature and CO atmosphere favored the volatilization of Cd. Based on the toxicity characteristic leaching procedure (TCLP) results, the pyrolysis treatment under both atmospheres enhanced the stability of Cd, and the leached Cd concentration of regenerated biochar obtained at high temperatures (>800 °C) was lower than 1 mg/L. Compared with the pristine biochar, the regenerated biochar demonstrated higher carbon content and pH, whereas the contents of oxygen and hydrogen declined, and exhibited promising sorption properties (35.79 mg/g). The atmosphere played an important role in modifying biochar properties and syngas composition. The N atmosphere facilitated CH production, whereas the CO atmosphere increased the proportion of CO. These results implied that pyrolysis can be a valuable and environmental-friendly strategy for the treatment and reuse of exhausted biochar sorbent.
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http://dx.doi.org/10.1016/j.scitotenv.2024.170712 | DOI Listing |
In this work, biochars were produced by pyrolysis of exhausted olive pomace and evaluated as low-cost adsorbents for the removal of methylene blue (MB) from aqueous solutions. The biochar obtained at 400 °C for 1 h, which exhibited the best adsorption performance, was characterized by FTIR, N adsorption-desorption isotherms, SEM-EDX, and proximate analysis, revealing a mesoporous structure with a relatively low specific surface area but enriched in surface functional groups, likely due to the partial degradation of lignocellulosic components. Adsorption experiments were conducted to optimize operational parameters such as solid particle size (2-3 mm), agitation speed (75 rpm), and bioadsorbent dosage (1 g per 0.
View Article and Find Full Text PDFSci Total Environ
March 2025
Department of Chemical Engineering, Indian Institute of Technology Roorkee, Uttarakhand, India. Electronic address:
The worsening environmental conditions, diminishing fossil fuel reserves, and increasing waste accumulation have redirected the attention of researchers and scientists towards the exploration of sustainable and non-exhaustive energy sources, as well as waste mitigation techniques. Among the various thermochemical technologies producing biofuels, hydrothermal liquefaction stands out as an effective technique for the simultaneous waste valorization and the production of sustainable biofuels. Under optimal conditions, hydrothermal liquefaction converts 70-80 % of feedstock energy into bio-oil, representing approximately 30-50 % of the feedstock's original mass.
View Article and Find Full Text PDFChemosphere
March 2025
Laboratory of Water, Biodiversity and Climate Change (EauBiodiCc), Faculty of Sciences Semlalia, University Cadi Ayyad, Marrakech, Morocco; National Centre for Studies and Research on Water and Energy (CNEREE), University Cadi Ayyad, Marrakech, Morocco. Electronic address:
Chemosphere
December 2024
Environmental Engineering Department, Egypt-Japan University of Science and Technology (E-JUST), Alexandria, 21934, Egypt.
While the industrial sectors have recently focused on producing bioplastic materials, the utilization of edible feedstocks and the generation of wastes and byproducts during the bioplastic synthesis process might delay achieving the environmental sustainability strategy. To overcome these limitations related to bioplastic industrialization, this study focuses on synthesizing bioplastics from waste sources, followed by recycling its end-of-life (e.g.
View Article and Find Full Text PDFInt J Phytoremediation
November 2024
Environmental Engineering Department, Egypt-Japan University of Science and Technology (E-JUST), Alexandria, Egypt.
While phytoremediation has been widely employed for greywater treatment, this system suffers from the transfer of considerable amounts of surfactants to the aquatic environment through partially treated effluent and/or exhausted plant disposal. Hence, this study focuses on greywater phytoremediation followed by recycling the spent plant for preparing an adsorbent material used as post-treatment. was used to operate a phytoremediation unit under 23 °C, 60% relative humidity, plant density (5-30 g/L), dilution (0-50%), pH (4-10), and retention time (3-15 days).
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