2001
DOI: 10.1007/bf02698300
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Adsorption equilibrium of solvent vapors on activated carbons

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Cited by 17 publications
(10 citation statements)
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“…Activated carbon exhibiting an excellent adsorption capacity, as effect of its large specific surface area and pore volume, is widely used as an adsorbent due to its low cost and great accessibility [2][3][4]6,10,12,14,16,18,20,22,23,25,28,29]. However, it is recognized that the activated carbon can present some disadvantages, e.g., inflammability, pore clogging, lower selectivity, inefficient regeneration [5,12,13,18,23,25,28].…”
Section: Introductionmentioning
confidence: 99%
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“…Activated carbon exhibiting an excellent adsorption capacity, as effect of its large specific surface area and pore volume, is widely used as an adsorbent due to its low cost and great accessibility [2][3][4]6,10,12,14,16,18,20,22,23,25,28,29]. However, it is recognized that the activated carbon can present some disadvantages, e.g., inflammability, pore clogging, lower selectivity, inefficient regeneration [5,12,13,18,23,25,28].…”
Section: Introductionmentioning
confidence: 99%
“…VOCs abatement techniques can be divided into two categories, i.e., destructive (thermal, catalytic, and photocatalytic oxidation, bio-filtration) and recuperative (adsorption, absorption, condensation, membrane separation) [1,8,9]. Adsorption onto porous materials is a well-established, highly selective, energy efficient, and relatively inexpensive technique employed for the removal and recovery of VOCs from air, especially at a low concentration [1,3,5,6,[10][11][12][13][14][15][16][17][18]. Porous materials having large specific surface area and pore volume, including activated carbon and its derivatives [1][2][3][4]6,10,14,16,[19][20][21][22], alumina [18], natural clay [18], natural and modified zeolites [11,[23][24][25][26], are the most frequently applied adsorbents.…”
Section: Introductionmentioning
confidence: 99%
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“…2,2,4-Trimethylpentane and toluene vapors were chosen as adsorbates. Equilibrium experiments were carried out at three different temperatures of 303.15, 323.15, and 343.15 K. Adsorption data of each hydrocarbon was fitted to the well-known isotherms such as the Langmuir equation and the Freundlich equation [5,6]. Furthermore, the surface energetic heterogeneity of the adsorbents was evaluated using the isosteric heat of adsorption based on the ClausiusClapeyron equation.…”
Section: Introductionmentioning
confidence: 99%