TY - JOUR
T1 - Theoretical Insight of Physical Adsorption for a Single-Component Adsorbent + Adsorbate System: I. Thermodynamic Property Surfaces
AU - Chakraborty, Anutosh
AU - Saha, Bidyut Baran
AU - Ng, Kim Choon
AU - Koyama, Shigeru
AU - Srinivasan, Kandadai
N1 - KAUST Repository Item: Exported on 2020-10-01
Acknowledged KAUST grant number(s): WBS R265-000286-597
Acknowledgements: The authors would like to thank King Abdullah University of Science & Technology (KAUST) for the generous financial support through the project (WBS R265-000286-597).
This publication acknowledges KAUST support, but has no KAUST affiliated authors.
PY - 2009/2/17
Y1 - 2009/2/17
N2 - Thermodynamic property surfaces for a single-component adsorbent + adsorbate system are derived and developed from the viewpoint of classical thermodynamics, thermodynamic requirements of chemical equilibrium, Gibbs law, and Maxwell relations. They enable us to compute the entropy and enthalpy of the adsorbed phase, the isosteric heat of adsorption, specific heat capacity, and the adsorbed phase volume thoroughly. These equations are very simple and easy to handle for calculating the energetic performances of any adsorption system. We have shown here that the derived thermodynamic formulations fill up the information gap with respect to the state of adsorbed phase to dispel the confusion as to what is the actual state of the adsorbed phase. We have also discussed and established the temperature-entropy diagrams of (i) CaCl 2-in-silica gel + water system for cooling applications, and (ii) activated carbon (Maxsorb III) + methane system for gas storage. © Copyright 2009 American Chemical Society.
AB - Thermodynamic property surfaces for a single-component adsorbent + adsorbate system are derived and developed from the viewpoint of classical thermodynamics, thermodynamic requirements of chemical equilibrium, Gibbs law, and Maxwell relations. They enable us to compute the entropy and enthalpy of the adsorbed phase, the isosteric heat of adsorption, specific heat capacity, and the adsorbed phase volume thoroughly. These equations are very simple and easy to handle for calculating the energetic performances of any adsorption system. We have shown here that the derived thermodynamic formulations fill up the information gap with respect to the state of adsorbed phase to dispel the confusion as to what is the actual state of the adsorbed phase. We have also discussed and established the temperature-entropy diagrams of (i) CaCl 2-in-silica gel + water system for cooling applications, and (ii) activated carbon (Maxsorb III) + methane system for gas storage. © Copyright 2009 American Chemical Society.
UR - http://hdl.handle.net/10754/599982
UR - https://pubs.acs.org/doi/10.1021/la803289p
UR - http://www.scopus.com/inward/record.url?scp=65249131634&partnerID=8YFLogxK
U2 - 10.1021/la803289p
DO - 10.1021/la803289p
M3 - Article
C2 - 19140706
SN - 0743-7463
VL - 25
SP - 2204
EP - 2211
JO - Langmuir
JF - Langmuir
IS - 4
ER -