Adsorption of Acetone and Cumene on Activated Carbon. I. Single-component Adsorption Equilibria of Acetone and Cumene on Supersorbon HS-4

Adsorption equilibrium data for the systems acetone/activated carbon and cumene/activated carbon measured over the pressure ranges 0.2–20 500 Pa and 2–420 Pa, respectively and over the temperature range 10–120°C have been fitted to the Langmuir, O'Brien–Myers and Toth isotherms, as well as the...

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Main Authors: Eva Besedova, Daniel Bobok
Format: Article
Language:English
Published: SAGE Publications 1995-03-01
Series:Adsorption Science & Technology
Online Access:https://doi.org/10.1177/026361749501200105
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author Eva Besedova
Daniel Bobok
author_facet Eva Besedova
Daniel Bobok
author_sort Eva Besedova
collection DOAJ
description Adsorption equilibrium data for the systems acetone/activated carbon and cumene/activated carbon measured over the pressure ranges 0.2–20 500 Pa and 2–420 Pa, respectively and over the temperature range 10–120°C have been fitted to the Langmuir, O'Brien–Myers and Toth isotherms, as well as the Dubinin-Astakhov equation. The best fit with the experimental data was obtained using the Toth isotherm and the Dubinin–Astakhov equation.
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spelling doaj.art-6f4ff58e6d84498d9cb112f575bc63652024-03-02T16:14:50ZengSAGE PublicationsAdsorption Science & Technology0263-61742048-40381995-03-011210.1177/026361749501200105Adsorption of Acetone and Cumene on Activated Carbon. I. Single-component Adsorption Equilibria of Acetone and Cumene on Supersorbon HS-4Eva Besedova0Daniel Bobok1Department of Chemical and Biochemical Engineering, Faculty of Chemical Technology, Slovak Technical University, Radlinského 9, 812 37 Bratislava, Slovakia.Department of Chemical and Biochemical Engineering, Faculty of Chemical Technology, Slovak Technical University, Radlinského 9, 812 37 Bratislava, Slovakia.Adsorption equilibrium data for the systems acetone/activated carbon and cumene/activated carbon measured over the pressure ranges 0.2–20 500 Pa and 2–420 Pa, respectively and over the temperature range 10–120°C have been fitted to the Langmuir, O'Brien–Myers and Toth isotherms, as well as the Dubinin-Astakhov equation. The best fit with the experimental data was obtained using the Toth isotherm and the Dubinin–Astakhov equation.https://doi.org/10.1177/026361749501200105
spellingShingle Eva Besedova
Daniel Bobok
Adsorption of Acetone and Cumene on Activated Carbon. I. Single-component Adsorption Equilibria of Acetone and Cumene on Supersorbon HS-4
Adsorption Science & Technology
title Adsorption of Acetone and Cumene on Activated Carbon. I. Single-component Adsorption Equilibria of Acetone and Cumene on Supersorbon HS-4
title_full Adsorption of Acetone and Cumene on Activated Carbon. I. Single-component Adsorption Equilibria of Acetone and Cumene on Supersorbon HS-4
title_fullStr Adsorption of Acetone and Cumene on Activated Carbon. I. Single-component Adsorption Equilibria of Acetone and Cumene on Supersorbon HS-4
title_full_unstemmed Adsorption of Acetone and Cumene on Activated Carbon. I. Single-component Adsorption Equilibria of Acetone and Cumene on Supersorbon HS-4
title_short Adsorption of Acetone and Cumene on Activated Carbon. I. Single-component Adsorption Equilibria of Acetone and Cumene on Supersorbon HS-4
title_sort adsorption of acetone and cumene on activated carbon i single component adsorption equilibria of acetone and cumene on supersorbon hs 4
url https://doi.org/10.1177/026361749501200105
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AT danielbobok adsorptionofacetoneandcumeneonactivatedcarbonisinglecomponentadsorptionequilibriaofacetoneandcumeneonsupersorbonhs4