Submitted:
13 May 2025
Posted:
14 May 2025
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Abstract
Keywords:
1. Introduction
2. Thermodynamic Functions of Lattice Gases of Polyatomics in One Dimension: Exact Solutions for Single Species and Mixtures
2.1. One-Dimensional Model of Non-Interacting Structured Particles
2.1.1. Exact Solution for Rigid Particles on a 1D-Lattice: Single Species
2.1.2. Exact Solution for Rigid Particles on 1D-Lattice: Binary Mixtures
2.1.3. Multilayer Adsorption in the Presence of Multisite Occupancy: Exact Solution for 1D Substrates
2.1.4. Multilayer Adsorption of Dimers
2.2. One-Dimensional Model of Interacting Structured Particles
2.2.1. Exact Solution for Laterally Interacting Particles on 1D-Lattic e
2.2.2. Exact Solution for Binary Mixtures of Interacting Polyatomics on 1D-Lattices
3. Thermodynamic Functions of Lattice Gases of Polyatomics in Two Dimensions: Analytical Approaches for Single Species and Mixtures
3.1. Two-Dimensional Model of Non-Interacting Structured Particles: Historical Developments
3.1.1. Flory-Huggins Approximation ()
3.1.2. Guggenheim–DiMarzio Approximation ()
3.2. Two-Dimensional Model of Non-Interacting Structured Particles: More Recent Approximations from Our Group
3.2.1. Extension to Higher Dimensions of the Exact Thermodynamic Functions in One Dimension ()
3.2.2. Fractional Statistics Thermodynamic Theory of Adsorption of Polyatomics ()
3.2.3. Occupation Balance Approximation ()
3.2.4. Semi-Empirical Adsorption Model for Polyatomics ()
3.2.5. Brief Introduction to Multiple Exclusion Statistics
3.3. Two-Dimensional Model of Non-Interacting (k-Mers–l-Mers) Binary Mixtures
3.3.1. Approximation
3.3.2. Approximation
3.3.3. Approximation
3.4. Multilayer Adsorption in the Presence of Multisite Occupancy: Theoretical Approach for 2D Substrates
4. Two-Dimensional Lattice Gases of Interacting Polyatomics
4.1. Mean-Field Approximation for Interacting k-Mers Adsorbed on 2D Substrates
4.2. Quasi-Chemical Approximation for Interacting k-Mers Adsorbed on 2D Substrates
4.2.1. General Expression of the Thermodynamic Functions in Terms of the Configurational Factor
4.3. Quasi-Chemical Approximation for Interacting Mixtures Adsorbed on 2D Substrates
- 1)
- 2)
- 3)
- 4)
6. Latest Developments, Part II: Multiple Exclusion Statistics Formulation for Mixtures
6.1. State Counting Approximation and Density of States for Mixtures with Multiple State Exclusion

6.2. Mixtures Statistical Thermodynamics
6.3. State Exclusion Spectrum Functions: Determination of Exclusion Correlation Parameters
6.4. The k-Mers Problem as a Mixture Model: Basic Definitions
7. Applications
7.1. Two-Dimensional Adsorption: Comparison Between Theory and Monte Carlo Simulations
7.2. Two-Dimensional Adsorption of Binary Mixtures: Comparison Between Theory and Monte Carlo Simulations
7.3. Two-Dimensional Adsorption of Interacting k-Mers: Comparison Between Theory and Monte Carlo Simulations
7.4. Application of to the Adsorption of and in Zeolites 13X and 5A: Determination of the Adsorption Configuration

7.5. Adsorption of Methane-Ethane Mixtures in Zeolites: Reversal Adsorption Phenomena
7.6. Alkanes Adsorbed in Carbon Nanotubes Bundles: Surface Area Characterization
- (1)
-
In this first approach (procedure A), we used the one-dimensional MBET equations for all four adsorbates to account for the linear geometry of the molecules. For methane, we employed the standard BET equation, which corresponds to the MBET expression for monomers. For ethane, we applied the exact 1-D MBET formula for dimers [Equation (342)]. For propane and butane, we utilized the same dimer equation but adjusted its parameters to fit the experimental data in the low-pressure, low-coverage regime—specifically, the same region typically used in BET analysis.Using Procedure A, the calculated specific surface areas for ethane, propane, and butane were consistently higher than those obtained using the BET method. In addition to producing improved results, this method remains relatively straightforward to implement.However, we also observed a consistent trend: as the length of the alkane chain increases, the derived specific surface area decreases. This behavior is illustrated in Figure 6, which includes data obtained from both this and other approaches.Although not perfect, the results from Procedure A represent a clear enhancement over the standard BET approach.
- 2)
-
The second strategy (procedure B) involved fitting the isotherm data for all four adsorbates to the approximate MBET expression developed for the two-dimensional case [Equation (209) in Section 3.4]In this formulation, is a constant that reflects both the interaction strength between the adsorbate and the substrate, as well as the connectivity of the adsorption lattice. The parameter k denotes the number of units in the k-mer molecule.The experimental adsorption isotherms are fitted to this model using the appropriate k value for each adsorbate—1 for methane, 2 for ethane, 3 for propane, and 4 for butane—within the same low-pressure range typically employed for BET analysis. Figure 55 shows the fit obtained for butane, which demonstrates excellent agreement with the data; similarly accurate fits were achieved for the other three alkanes. The fits yield values for the monolayer capacity, , which are subsequently used to compute the specific surface area of the sample.
7.7. Crystal Growth from Aqueous Solution in the Presence of Structured Impurities
- Case HCOOH: Equation (355) was used as fitting function, with and as adjustable parameter.
- Case CH3COOH: Equation (356) was used as fitting function, with and as adjustable parameter.
- Case C2H5COOH: Equation (357) was used as fitting function, with and as adjustable parameter.
- Case C3H7COOH: Equation (358) was used as fitting function, with and as adjustable parameter.
7.8. Application to k-Mers Phase Transitions
7.8.1. Basic Definitions
7.8.2. Entropy Surface, Equilibrium Path, and Order Parameter
7.8.3. Generalized Density of States Function in Multiple Exclusion Statistics
7.8.4. Nematic-Phase Density Branches and Phase Transitions
7.8.5. State Exclusion Spectrum Functions of k-Mers: Coverage Dependence


8. Monte Carlo Simulation Method Applied to the Problem of Adsorption with Multisite Occupancy
8.1. Metropolis MC Algorithms for Adsorption of Interacting k-Mers
8.1.1. Grand Canonical Ensemble
- i)
- set the value of the chemical potential and the temperature T;
- ii)
- choose randomly a linear k-uple of nearest-neighbor sites.
- iii)
- if the k sites selected in are empty, an attempt is made to deposit a rod with probability ; if the k sites selected in are occupied by units belonging to the same k-mer, an attempt is made to desorb this k-mer with probability and otherwise, the attempt is rejected. Here, and represent the probabilities of transition from a state with N particles to a new state with or particles, respectively. Following the Metropolis scheme [174], these probabilities are given by , where is the difference between the Hamiltonians of the final and initial states.
- iv)
- repeat steps M times.
8.1.2. Canonical Ensemble
- i)
- set the value of the temperature T;
- ii)
- set the value of the coverage, , by adsorbing linear molecules onto the lattice, each molecule occupying k adsorption sites;
- iii)
- a k-mer and a linear k-uple of empty sites are randomly selected, and their positions are established. Then, an attempt is made to interchange its occupancy state with probability given by the Metropolis rule [174]:where is the difference between the Hamiltonians of the final and initial states;
- iv)
- a k-mer is randomly selected. Then, a displacement to nearest-neighbor positions is attempted (following the Metropolis scheme), by either jumps along the k-mer axis or reptation by rotation around a unity of the k-mer. This procedure (diffusional relaxation) must be allowed in order to reach equilibrium in a reasonable time; and
- v)
- repeat steps iii)-iv) M times.
8.2. Parallel Tempering MC Algorithm for Adsorption of Interacting k-Mers
Replica-update.
Replica-exchange.
8.3. Parallel Tempering MC Algorithm for Adsorption of Binary Mixtures of Interacting Species of Polyatomics
Replica-update.
Replica-exchange.
8.4. Improving the Update Algorithm Through the Use of Lists of Full and Empty k-Uples
8.5. Non-Local Update Kundu’s Algorithm for Adsorption of Non-Interacting Large k-Mers (Only Excluded Volume Interaction)
8.6. Thermodynamic Integration Method in Canonical Ensemble: Artificial Hamiltonian Method
9. Conclusions and Future Perspectives
Author Contributions
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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| 1 | The simulations have been performed for chains of sites and periodic boundary conditions. |
| 2 | This adsorption field is usually represented by a lattice of adsorption sites although in the case of particles or molecules composed by more than one elementary unit there is not a one-to-one correspondence between an equilibrium state and a lattice as will be made clear latter. |
| 3 | It is worth to note that in general adsorbed molecules may adopt different configurations as the density increases. In this case the values obtained for g from experiments will depend on the pressure range analyzed, according to the general form of Equation (124). In turns, a relates to the low density limit , . |
| 4 | If it is assumed that each dimer is independent from the neighboring ones, each dimer excludes states out of total
|
| 5 | The term is subtracted since the total number of nearest-neighbor pairs, , includes the bonds belonging to the N adsorbed k-mers. |
| 6 | The solution is discarded for physical reasons. |
| 7 | Even in the simplest case of single dimers on M sites, there not exist the exact form of in two (or more) dimensions. |
| 8 | Typical examples include lattice gases with excluded volume interactions, where particles occupy multiple sites depending on their shape and size. |
| 9 | Note that includes the occupied state itself. |
| 10 |
accounts only for the states excluded by particle j, not by particles . The recursion can be interpreted as representing the most probable configurations at thermodynamic equilibrium. |
| 11 | In principle, one could consider . The assumption corresponds to a first-order approximation in statistics [17]. |
| 12 | |
| 13 | This is a restrictive condition implying that the entropy of species i vanishes at its saturation . A more general condition is discussed in Section 7.8.3. |
| 14 | See Ref. [19] for a general procedure to determine . |
| 15 | In one dimension, the reduces to the exact solution for interacting chains adsorbed flat on a one-dimensional lattice. With respect to , a characteristic Van der Waals loop appears in the isotherm under attractive interactions, erroneously predicting a phase transition for . For strong repulsive interactions, the deviates from the exact results and fails to reproduce the plateau observed in the adsorption isotherm. These limitations can be better understood through the entropy per site. The key assumption of the is that both the configurational degeneracy and the average nearest-neighbor interaction energy are treated as if molecules are randomly distributed across the lattice. As a result, the entropy per site becomes independent of w and takes the form given by Equation (13). |
| 16 | For , cannot be explicitly written in terms of . In this case, the calculations can be done with any standard mathematics software package. |
| 17 | As in the Kubota and Mullin model [168], molecular configuration in the adsorbed state is incorporated through the adsorption constant . |
| 18 | We assume that in any macroscopic region V filled with particles of species 1, the average number of self-excluded states is , and analogously represents the cross-excluded states from species 2 on species 1. |



































































| / | / | |
| (mol. / g) | 0.41 | 0.41 |
| (mmHg−1) | 3.5 | 0.48 |
| (mmHg−1) | 1.6 | 0.6 |
| System | k | m | g | D(%) | |||||
| 2 | 2 | 4 | 3.10 | 0.72 | 5.60 | ||||
| 3 | 1 | 3 | 5.75 | 6.94 | 1.27 | 2.08 |
| sample | type | weight (g) | gas | area/mol on graphite () | isotherm temp (K) |
| SWNTs | HiPco | 0.1727 | methane | 15.4 [145] | 77 |
| SWNTs | HiPco | 0.325 | ethane | 21 [146] | 165 |
| SWNTs | HiPco | 0.325 | propane | 28.8 [147] | 190 |
| SWNTs | HiPco | 0.325 | butane | 32.7 [146] | 220 |
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