2009
DOI: 10.1016/j.jcis.2009.01.055
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Modeling adsorption of liquid mixtures on porous materials

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Cited by 18 publications
(16 citation statements)
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“…The key idea of MPTA is that chemical potential of a component in a mixture is contributed by a bulk phase described by EOS and a potentialenergy contribution depending on the distance to the adsorbent (Monsalvo and Shapiro 2007). With simple assumption of adsorp-tion potential and adjustable parameters, MPTA shows good agreement with experimental data in multicomponent adsorption in porous media [Shapiro and Stenby (1998); Monsalvo and Shapiro (2007;2009a,2009b]. Although the properties of adsorbates can be described by an EOS in macropores; the properties in micropores (<2 nm) are completely different from those in the bulk.…”
Section: Introductionmentioning
confidence: 80%
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“…The key idea of MPTA is that chemical potential of a component in a mixture is contributed by a bulk phase described by EOS and a potentialenergy contribution depending on the distance to the adsorbent (Monsalvo and Shapiro 2007). With simple assumption of adsorp-tion potential and adjustable parameters, MPTA shows good agreement with experimental data in multicomponent adsorption in porous media [Shapiro and Stenby (1998); Monsalvo and Shapiro (2007;2009a,2009b]. Although the properties of adsorbates can be described by an EOS in macropores; the properties in micropores (<2 nm) are completely different from those in the bulk.…”
Section: Introductionmentioning
confidence: 80%
“…In principle, the behavior of confined-fluid phase is obtained by equaling the chemical potentials of bulk and adsorbed phase, which is described by the EOS and fluid/solid potential (Ustinov and Do 2003). Shapiro and Stenby (1998) and Monsalvo and Shapiro (2007;2009a, 2009b developed a multicomponent potential theory of adsorption (MPTA) to study mixture adsorption in porous materials. The key idea of MPTA is that chemical potential of a component in a mixture is contributed by a bulk phase described by EOS and a potentialenergy contribution depending on the distance to the adsorbent (Monsalvo and Shapiro 2007).…”
Section: Introductionmentioning
confidence: 99%
“…[21][22][23] MPTA has been applied to model adsorption of gas and liquid mixtures on absorbent like activated carbons and silica gels. 22,24,25 Recently, Bartholdy et al. 26 compared MPTA with Langmuir and IAST on prediction of multicomponent gas adsorption with emphasis on water and other polar gases and polar solids.…”
Section: Introductionmentioning
confidence: 99%
“…Several validations and comparisons of adsorption models for different adsorbents can be found in the literature. MPTA has been applied to model adsorption of gas and liquid mixtures on absorbent such as activated carbons and silica gels. ,, Recently, Bartholdy et al compared MPTA with Langmuir and IAST on prediction of multicomponent gas adsorption with emphasis on water and other polar gases and polar solids. In particular, for adsorption on organic-rich shales and coal, Clarkson and Hagshenas compared the simple Langmuir and Dubinin–Radushkevich (DR) equations and a 2D-EoS model for pure component adsorption and provided a prediction for binary mixtures.…”
Section: Introductionmentioning
confidence: 99%
“…The PTA model was generalized to MPTA for gas mixtures adsorption by Shapiro, Stenby, and Monsalvo [14,16]. The MPTA model supposes that the fluid-surface interaction is entirely described by a local potential field , generated by the surface [17,18]. A common choice for this purpose is the Dubinin-Radushkevich-Astakhov [19][20][21] potential (DRA), given by where 0 and z 0 are the characteristic energy of adsorption and the limiting micropore volume, respectively.…”
Section: Pure Gas Mpta Modelmentioning
confidence: 99%