2023
DOI: 10.1590/1678-4324-2023210125
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Development of Adsorbent Materials Using Residue from Coffee Industry and Application in Food dye Adsorption Processes

Abstract: The aim of this study was to develop an adsorbent from coffee husk, residue from the coffee industry by different activation methods and to evaluate its application in the treatment of effluent containing synthetic Ponceau 4R dye. The activations were with phosphoric acid and zinc chloride, then the samples were characterized in terms of physical and chemical composition, structure and morphology, thermal behavior and kinetic and thermodynamic study. Regarding the characterization of the material, the activati… Show more

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Cited by 7 publications
(6 citation statements)
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References 45 publications
(70 reference statements)
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“…At 40 • C, 50 • C, and 60 • C, the R 2 values of the pseudo-second-order kinetic model were more than 0.99, indicating that the adsorption of modified wheat bran fiber on Congo red was more consistent with the pseudo-second-order kinetic model. Many studies on the dye adsorption of chemically modified agricultural waste [39] also found that the dye adsorption processes were better suited to the pseudo-second-order kinetic model than the pseudo-first-order kinetic model. As for the calculated Q e , at 40 • C, 50 • C, and 60 • C, the calculated Q e values of the pseudo-second-order kinetic model were closer to the experimental results, while the calculated Q e values fitted by the pseudo-first-order kinetic model were quite different from the experimental values.…”
Section: Adsorption Kineticsmentioning
confidence: 99%
“…At 40 • C, 50 • C, and 60 • C, the R 2 values of the pseudo-second-order kinetic model were more than 0.99, indicating that the adsorption of modified wheat bran fiber on Congo red was more consistent with the pseudo-second-order kinetic model. Many studies on the dye adsorption of chemically modified agricultural waste [39] also found that the dye adsorption processes were better suited to the pseudo-second-order kinetic model than the pseudo-first-order kinetic model. As for the calculated Q e , at 40 • C, 50 • C, and 60 • C, the calculated Q e values of the pseudo-second-order kinetic model were closer to the experimental results, while the calculated Q e values fitted by the pseudo-first-order kinetic model were quite different from the experimental values.…”
Section: Adsorption Kineticsmentioning
confidence: 99%
“…The amount adsorbed reflects the adsorption capacity of the adsorbent on particular operating parameters. 119 Different kinetic models can describe the adsorption process. Al-Ghouti and Da'ana 32 report that it is possible to find more than 25 of these models in the literature, each based on theoretical and experimental considerations.…”
Section: Kinetic Profile Of Biocompoundsmentioning
confidence: 99%
“…The period required to reach this state is called the equilibrium time. The amount adsorbed reflects the adsorption capacity of the adsorbent on particular operating parameters 119 …”
Section: Application Of Adsorbents For Detoxification and Purificationmentioning
confidence: 99%
“…In addition to AC, various adsorbent materials have strong potential for the extraction, separation, and purification of components in an aqueous phase. These materials have chemical and structural properties that may favor the removal of highly toxic organic components 35,36 …”
Section: Introductionmentioning
confidence: 99%
“…These materials have chemical and structural properties that may favor the removal of highly toxic organic components. 35,36 Silica-based adsorbents are widely used for cleaning aqueous solutions in solid-phase extraction. 37 Silica modified with octadecyl groups improves the material's polarity in the extraction and separation of polar components.…”
Section: Introductionmentioning
confidence: 99%