In this work, the inverse fluidized-bed bio-adsorption column is applied for the first time and is demonstrated using the torrefied rice husk (TRH) for the removal of methylene blue from the solution. The bio-adsorbents were characterized by BET, FI-IR, and SEM. The inverse fluidized-bed adsorption column using TRH becomes saturated in the 95-min continuous adsorption, during which the breakthrough time is 22 min, the overall MB removal (R) is 84%, and the adsorption capacity (Q) on the TRH is 6.82 mg g. These adsorption characteristics are superior to those in the fixed-bed adsorption column (R of 52% and Q of 2.76 mg g) at a lower flow rate (100 vs. 283 cm min). Torrefaction of RH significantly increases the surface area (28 vs. 9 m g) and enhances the surface functional groups, leading to an improved maximum equilibrium adsorption amount from 21.5 to 38.0 mg g according to Langmuir model in the batch adsorption system. Besides, the increased Q on the TRH is also obtained in the inverse fluidized-bed (5.25 vs. 2.77 mg g, 89% higher) and the fixed-bed (2.76 vs. 1.53 mg g, 80% higher) adsorption columns compared to that on the RH.
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http://dx.doi.org/10.1016/j.chemosphere.2021.131907 | DOI Listing |
Pharmaceutics
June 2024
Laboratory of Pharmaceutical Technology, Department of Pharmaceutics, Ghent University, Ottergemsesteenweg 460, 9000 Ghent, Belgium.
Binder selection is a crucial step in continuous twin-screw wet granulation (TSWG), as the material experiences a much shorter residence time (2-40 s) in the granulator barrel compared to batch-wise granulation processes. Polyvinyl alcohol (PVA) 4-88 was identified as an effective binder during TSWG, but the potential of other PVA grades-differing in polymerization and hydrolysis degree-has not yet been studied. Therefore, the aim of the current study was to evaluate the potential of different PVA grades as a binder during TSWG.
View Article and Find Full Text PDFEnviron Sci Pollut Res Int
October 2023
Department of Biochemical Engineering and Biotechnology, Indian Institute of Technology Delhi, Hauz Khas, New Delhi, 110016, India.
A critical evaluation of strategies used for reducing start-up time and biological wastewater treatment using an inverse fluidized bed reactor (IFBR) was done. The start-up of an IFBR is one of the most important, time-consuming, and limiting steps in wastewater treatment using biofilm reactors. Evaluation of different strategies used by various researchers is helpful in future research works with this reactor.
View Article and Find Full Text PDFChemosphere
January 2022
Green Chemical Reaction Engineering, Engineering and Technology Institute Groningen, University of Groningen, Nijenborgh 4, 9747, AG, Groningen, The Netherlands; CoRe Pro, Colijnlaan 21, 9722, PJ, Groningen, The Netherlands. Electronic address:
In this work, the inverse fluidized-bed bio-adsorption column is applied for the first time and is demonstrated using the torrefied rice husk (TRH) for the removal of methylene blue from the solution. The bio-adsorbents were characterized by BET, FI-IR, and SEM. The inverse fluidized-bed adsorption column using TRH becomes saturated in the 95-min continuous adsorption, during which the breakthrough time is 22 min, the overall MB removal (R) is 84%, and the adsorption capacity (Q) on the TRH is 6.
View Article and Find Full Text PDFJ Environ Manage
December 2020
Department of Biochemical Engineering and Biotechnology, Indian Institute of Technology Delhi, 110016, New Delhi, India.
The comparative performance of an inverse fluidized bed reactor (IFBR) having high density polyethylene beads as carrier materials for biofilm formation and a continuous stirred tank reactor (CSTR), both maintaining autotrophic denitrification using biogenic sulphur (ADBIOS) in the absence and presence of nickel (Ni), was studied. The reactors were compared in terms of NO-N and NO-N removal and SO-S production throughout the study. A simulated wastewater with an inlet NO-N concentration of 225 mg/L and a decreasing concentration of biogenic sulphur (bio-S) from 1.
View Article and Find Full Text PDFSci Total Environ
May 2020
Department of Chemical and Biochemical Engineering, University of Western Ontario, London, ON N6A 5B9, Canada.
The performance of a lab-scale integrated anoxic and aerobic inverse fluidized bed bioreactors (IFBBR) for biological nutrient removal from synthetic municipal wastewater was studied at chemical oxygen demand (COD) loading rates of 0.34-2.10 kg COD/(m-d) and nitrogen loading rates of 0.
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