Generalized gas-solid adsorption modeling: Single-component equilibria
Abstract
Over the last several decades, modeling of gas–solid adsorption at equilibrium has generally been accomplished through the use of isotherms such as the Freundlich, Langmuir, Tóth, and other similar models. While these models are relatively easy to adapt for describing experimental data, their simplicity limits their generality to be used with many different sets of data. This limitation forces engineers and scientists to test each different model in order to evaluate which one can best describe their data. Additionally, the parameters of these models all have a different physical interpretation, which may have an effect on how they can be further extended into kinetic, thermodynamic, and/or mass transfer models for engineering applications. Therefore, it is paramount to adopt not only a more general isotherm model, but also a concise methodology to reliably optimize for and obtain the parameters of that model. A model of particular interest is the Generalized Statistical Thermodynamic Adsorption (GSTA) isotherm. The GSTA isotherm has enormous flexibility, which could potentially be used to describe a variety of different adsorption systems, but utilizing this model can be fairly difficult due to that flexibility. To circumvent this complication, a comprehensive methodology and computer code has been developed that canmore »
- Authors:
-
- Georgia Institute of Technology, Atlanta, GA (United States)
- Georgia Institute of Technology, Atlanta, GA (United States); Oak Ridge National Lab. (ORNL), Oak Ridge, TN (United States)
- Oak Ridge National Lab. (ORNL), Oak Ridge, TN (United States)
- Publication Date:
- Research Org.:
- Oak Ridge National Laboratory (ORNL), Oak Ridge, TN (United States)
- Sponsoring Org.:
- Work for Others (WFO); USDOE
- OSTI Identifier:
- 1185606
- Alternate Identifier(s):
- OSTI ID: 1249816
- Grant/Contract Number:
- AC05-00OR22725
- Resource Type:
- Accepted Manuscript
- Journal Name:
- Fluid Phase Equilibria
- Additional Journal Information:
- Journal Volume: 388; Journal Issue: 2; Journal ID: ISSN 0378-3812
- Publisher:
- Elsevier
- Country of Publication:
- United States
- Language:
- English
- Subject:
- 97 MATHEMATICS AND COMPUTING; gas solid equilibrium; computer modeling; adsorption isotherm; statistical thermodynamics
Citation Formats
Ladshaw, Austin, Yiacoumi, Sotira, Tsouris, Costas, and DePaoli, David W. Generalized gas-solid adsorption modeling: Single-component equilibria. United States: N. p., 2015.
Web. doi:10.1016/j.fluid.2015.01.003.
Ladshaw, Austin, Yiacoumi, Sotira, Tsouris, Costas, & DePaoli, David W. Generalized gas-solid adsorption modeling: Single-component equilibria. United States. https://doi.org/10.1016/j.fluid.2015.01.003
Ladshaw, Austin, Yiacoumi, Sotira, Tsouris, Costas, and DePaoli, David W. Wed .
"Generalized gas-solid adsorption modeling: Single-component equilibria". United States. https://doi.org/10.1016/j.fluid.2015.01.003. https://www.osti.gov/servlets/purl/1185606.
@article{osti_1185606,
title = {Generalized gas-solid adsorption modeling: Single-component equilibria},
author = {Ladshaw, Austin and Yiacoumi, Sotira and Tsouris, Costas and DePaoli, David W.},
abstractNote = {Over the last several decades, modeling of gas–solid adsorption at equilibrium has generally been accomplished through the use of isotherms such as the Freundlich, Langmuir, Tóth, and other similar models. While these models are relatively easy to adapt for describing experimental data, their simplicity limits their generality to be used with many different sets of data. This limitation forces engineers and scientists to test each different model in order to evaluate which one can best describe their data. Additionally, the parameters of these models all have a different physical interpretation, which may have an effect on how they can be further extended into kinetic, thermodynamic, and/or mass transfer models for engineering applications. Therefore, it is paramount to adopt not only a more general isotherm model, but also a concise methodology to reliably optimize for and obtain the parameters of that model. A model of particular interest is the Generalized Statistical Thermodynamic Adsorption (GSTA) isotherm. The GSTA isotherm has enormous flexibility, which could potentially be used to describe a variety of different adsorption systems, but utilizing this model can be fairly difficult due to that flexibility. To circumvent this complication, a comprehensive methodology and computer code has been developed that can perform a full equilibrium analysis of adsorption data for any gas-solid system using the GSTA model. The code has been developed in C/C++ and utilizes a Levenberg–Marquardt’s algorithm to handle the non-linear optimization of the model parameters. Since the GSTA model has an adjustable number of parameters, the code iteratively goes through all number of plausible parameters for each data set and then returns the best solution based on a set of scrutiny criteria. Data sets at different temperatures are analyzed serially and then linear correlations with temperature are made for the parameters of the model. The end result is a full set of optimal GSTA parameters, both dimensional and non-dimensional, as well as the corresponding thermodynamic parameters necessary to predict the behavior of the system at temperatures for which data were not available. It will be shown that this code, utilizing the GSTA model, was able to describe a wide variety of gas-solid adsorption systems at equilibrium.In addition, a physical interpretation of these results will be provided, as well as an alternate derivation of the GSTA model, which intends to reaffirm the physical meaning.},
doi = {10.1016/j.fluid.2015.01.003},
journal = {Fluid Phase Equilibria},
number = 2,
volume = 388,
place = {United States},
year = {Wed Jan 07 00:00:00 EST 2015},
month = {Wed Jan 07 00:00:00 EST 2015}
}
Web of Science
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Works referencing / citing this record:
Isotherms for Water Adsorption on Molecular Sieve 3A: Influence of Cation Composition
journal, July 2015
- Lin, Ronghong; Ladshaw, Austin; Nan, Yue
- Industrial & Engineering Chemistry Research, Vol. 54, Issue 42
Computationsl modelling of dimethyl ether separation and steam reforming in fluidized bed reactors
dissertation, January 2016
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