Skip to main content
ACS AuthorChoice logoLink to ACS AuthorChoice
. 2022 Jun 17;38(26):7989–8002. doi: 10.1021/acs.langmuir.2c00753

Surface Area Estimation: Replacing the Brunauer–Emmett–Teller Model with the Statistical Thermodynamic Fluctuation Theory

Seishi Shimizu †,*, Nobuyuki Matubayasi
PMCID: PMC9261182  PMID: 35715002

Abstract

graphic file with name la2c00753_0011.jpg

Surface area estimation using the Brunauer–Emmett–Teller (BET) analysis has been beset by difficulties. The BET model has been applied routinely to systems that break its basic assumptions. Even though unphysical results arising from force-fitting can be eliminated by the consistency criteria, such a practice, in turn, complicates the simplicity of the linearized BET plot. We have derived a general isotherm from the statistical thermodynamic fluctuation theory, leading to facile isotherm fitting because our isotherm is free of the BET assumptions. The reinterpretation of the monolayer capacity and the BET constant has led to a statistical thermodynamic generalization of the BET analysis. The key is Point M, which is defined as the activity at which the sorbate–sorbate excess number at the interface is at its minimum (i.e., the point of strongest sorbate–sorbate exclusion). The straightforwardness of identifying Point M and the ease of fitting by the statistical thermodynamic isotherm have been demonstrated using zeolite 13X and a Portland cement paste. The adsorption at Point M is an alternative for the BET monolayer capacity, making the BET model and its consistency criteria unnecessary. The excess number (i) replaces the BET constant as the measure of knee sharpness and monolayer coverage, (ii) links macroscopic (isotherms) to microscopic (simulation), and (iii) serves as a measure of sorbate–sorbate interaction as a signature of sorption cooperativity in porous materials. Thus, interpretive clarity and ease of analysis have been achieved by a statistical thermodynamic generalization of the BET analysis.

Introduction

Specific surface area is one of the major characteristics of materials as adsorbents.15 This quantity has been estimated from the adsorption of probe gas sorbates with the help of isotherm models, most commonly by the Brunauer–Emmett–Teller (BET) model.6,7 (We use the term “estimation” throughout, appreciating its approximate nature due to the assumptions involved.) Here, the “BET surface area” is defined as the BET monolayer capacity (i.e., “the amount needed to cover the surface with a complete monolayer of atoms or molecules in a close-packed array”8) multiplied by the molecular cross-sectional area of the adsorbate.9,10 Despite its widespread use,13,11,12 concerns persist about the validity and accuracy of the BET surface area, which will be summarized below, followed by our approach for clarification and resolution.

Calculated Surface Area Differs from Sorbate to Sorbate

The BET surface areas are often different from one probe sorbate to another, such as nitrogen and water.11,12 According to a systematic comparison for hardened Portland cement pastes, the estimated surface area using nitrogen gas as a sorbate is consistently lower than the one obtained from water vapor.12 For food11 and microcrystalline cellulose,13 the BET surface areas from water can be an order of magnitude larger than their nitrogen-based counterparts. Such a difference has been attributed to a larger molecular size of nitrogen,12 to the penetration of water and different states of the sorbed water,13 or used as a piece of evidence to question whether the water monolayer really exists.11

Reality of the BET Model Has Been Questioned

The BET model is based on a set of assumptions that include (1) adsorption on a uniform surface, (2) each adsorbed molecule in a layer is a potential adsorption site for the next layer, (3) no steric limitation on the thickness of the multilayer, (4) no interaction between the molecules in the same layer, and (5) the energy of adsorption on the first layer is higher than the rest (Figure 1a).3 However, as has been pointed out, “[t]he BET model appears to be unrealistic in a number of respects. For example, in addition to the Langmuir concept of an ideal localized monolayer adsorption, it is assumed that all the adsorption sites for multilayer adsorption are energetically identical and that all layers after the first have liquid-like properties.”2 Furthermore, Rouquerol et al. have even stated that “the BET model does not provide a realistic description of any known physisorption system.”2 Hence, the previous discussions on the validity and foundation of the BET surface area have centered around the validity of these assumptions, especially for porous and granular systems.3,1113

Figure 1.

Figure 1

Difference between the previous isotherm models (a) and our statistical thermodynamic approach (b,c). (a) Langmuir model assumes monolayer adsorption on a uniform surface with a binding constant (the Langmuir constant). The BET model assumes each adsorbed molecule as a potential adsorption site for the next layer and neglects interaction between the sorbates in the same layer. The BET constant is related (exponentially) to the difference in binding energies between the first and outer layers. (b) Our statistical thermodynamic approach does not involve any assumptions on binding layers, constants, or the mode of sorbate interaction. Instead, it is based on the difference in sorbate numbers between the system with the interface (left) and the gas and sorbent reference systems (right). (c) Statistical thermodynamic isotherm (eq 7) can be derived by incorporating the sorbate-interface (blue), sorbate–sorbate (green), and sorbate triplet (orange) interactions in the Maclaurin expansion (eq 6). Note that the sorbate–sorbate and sorbate triplet interactions captured using the pair and triplet number correlations are influenced by the presence of the interface (sorbents). Our theory is valid regardless of sorbate and sorbent molecular size and shape. For the precise definitions of A0, B0, and C0, see eqs 8 and 9 and ref (22).

Consistency Criteria are Needed to Remove Unphysical Results from the BET Model

The BET model has a simple mathematical form; hence, the monolayer capacity and the BET constant can be determined graphically from the linearized BET plot.3 However, the BET plot often exhibits linearity over a limited range of sorbate activity (relative pressure).3,10 Moreover, identifying the linear region of the BET plot can be subjective.3,10 Such long-standing difficulties in fitting the BET model to experimental isotherms have led to the following consistency criteria (Figure 2) that3,10,14,15

Figure 2.

Figure 2

Schematic diagram for a BET isotherm and the consistency criteria. (a) Amount of sorption ⟨n2⟩ against the sorbate activity a2 (or equivalently, the relative pressure p/po) for the BET model with CB = 80. Point B, or the knee of the isotherm, is hard to identify by visual inspection. Hence, the consistency criterion D, that is, ⟨n2⟩ = nm at Inline graphic, is employed. (b) Linearized BET plot guarantees that the BET constant is positive (criterion A), and the BET plot is linear at the activity corresponding to the nm (criterion C). (c) Increase in ⟨n2⟩(1 – a2) at the a2 corresponding to nm (the red dotted line in (a)) satisfies the criterion B.

A. the BET constant CB must be positive (Figure 2b);

B. “the application of the BET equation should be restricted to the range where the term n(1 – p/p0)continuously increases with [the sorbate activity] p/p010 (where n is the amount of sorption, Figure 2c);

C. the value of the monolayer capacity “should correspond to a relative pressure p/p0 falling within the selected linear region” (Figure 2b);14 and

D. “[t]he relative pressure corresponding to the monolayer loading calculated from BET theory [Inline graphic] should be equal to the pressure determined in criterion [C],”14 with the tolerance of 20% (Figure 2a).3,14

These criteria have been introduced to eliminate unphysical BET parameters, yet their intricacy has made the simple linearized BET plot cumbersome to apply. In addition, the applicability of the criteria has been a matter of debate recently.14,15 We will show that such difficulty comes from the restrictive BET model assumption, and its removal makes the analysis of isotherms straightforward.

Measuring the Monolayer Capacity from the Knee

A core idea of BET is that the monolayer coverage represents the amount of sorption at the knee:13,6,11,12,16 “If the knee of the isotherm is sharp, the uptake at Point B—the beginning of the middle quasilinear section—is usually considered to represent the completion of the monomolecular layer (monolayer) and the beginning of the formation of the multimolecular layer (multilayer).”2 However, because the knee is often ill-defined, it has become usual to derive the capacity from the linearized BET plot. For example, an IUPAC report suggests a method “to obtain by visual inspection the uptake at Point B, which usually agrees with [the monolayer capacity] derived from [the linearized BET plot] within a few percent”,9 while admitting that “Point B is not itself amenable to any precise mathematical description, the theoretical significance of the amount adsorbed at Point B is uncertain.”9 Even though “the relative pressure [...] for the monolayer capacity can be recalculated from the value of [the BET constant] through the BET equation”3 and has been used as a criterion for consistency,3,15 its underlying significance beyond its definition has remained unclear. As we will show later, stepping away from the BET formalism allows the direct and unambiguous method for identifying the knee point in a mathematically precise manner with clear physical insights, even for knees that are not sharp, thereby restoring the intuitive idea of the knee to its proper place.

Applicability of the BET and GAB Models is Much Wider than Their Original Assumptions

Non-planar, granular, and powder systems with moisture absorption have been modeled routinely by the BET model and by its extension, the Guggenheim–Anderson–de Boer (GAB) model,1719 even though these models were originally derived exclusively for adsorption, assuming planar surfaces with successive adsorption onto multiple layers.20 This contradiction was resolved by the current authors using statistical thermodynamics (Figure 1).2125 A general isotherm, which contains the BET and GAB models as its special cases,22 has been derived from a Maclaurin expansion of the sorbate–sorbate interaction (quantified via the Kirkwood–Buff integral) at the dilute limit, incorporating up to sorbate pair and triplet contributions (Figure 1b,c). This has fulfilled “the need to examine the limitations of the BET method and in particular to attempt to define the conditions which govern its application”;2 the wide applicability of the BET or GAB comes from the sorbate pair and triplet contribution instead of the planar multilayer assumption, rationalizing why the BET and GAB models are widely applicable beyond their original assumptions.22 In the current paper, we build on those insights to address the problems with surface area estimation.

Regional Isotherms

Crucial for BET surface area estimation is the identification of the region of sorbate activity (relative pressure) within which the BET plot is linear. As pointed out by IUPAC, “the range of linearity of the BET plot is always restricted to a limited part of the isotherm – usually not above [a2] ∼ 0.3”,26 and typically the linear region is chosen between 0.05 and 0.3.3,10 However, ambiguity persists on how to choose the range of linearity, leading to the multiplicity of the BET parameters.3 Moreover, some regions of linearity yield negative monolayer capacity.3 This highlights a contradiction: while the BET model is agreed to be applicable to a limited range of sorbate activity (relative pressure), extrapolation to zero activity in the BET plot, beyond this limited range, is indispensable for evaluating the BET parameters.

Our Strategy

The debate on the foundation and legitimacy of the BET surface area was centered around the validity of the BET model assumptions and the range of sorbate activity (relative pressure) to which they are applicable. Based on our recent clarification on the foundation of the BET model based on statistical thermodynamics,22 a new and alternative approach, consisting of the following three steps, is necessary:

  • I

    to start from the universal statistical thermodynamic principles of sorption (Figure 1b),

  • II

    to translate what the BET monolayer capacity and the BET surface area mean in the language of statistical thermodynamics and molecular interaction (Figure 1c), and

  • III

    to overcome the difficulties arising from applying the equation for the entire isotherm to regional isotherm data, namely, to eliminate the need for extrapolating to a zero activity limit.

These steps will lead to a redefinition of interfacial coverage and sorbate packing in the framework of the statistical thermodynamic fluctuation theory. The new method to analyze isotherms will be more straightforward because the restrictive BET model assumption and the consistency criteria are no longer necessary.

Theory

Overview

Here, we outline what will be achieved in this section to address the particular issues of the BET model identified in the Introduction. Each bullet point refers to a subsection within the Theory section.

  • A rigorous statistical thermodynamic fluctuation approach to sorption will be presented, linking the gradient of an isotherm to sorbate number fluctuation. This is in contrast to the existing isotherms, such as the BET model, constructed on the assumptions of adsorption sites, adsorption layers, and association constants (Figure 1a). We derive the statistical thermodynamic isotherm via the Maclaurin expansion, incorporating sorbate-interface, sorbate–sorbate, and sorbate triplet interactions (Figure 1b,c).

  • Re-interpreting the BET model from the statistical thermodynamic fluctuation theory will be made possible because the BET model is a restricted case of the statistical thermodynamic isotherm. This enables us to attribute a statistical thermodynamic reinterpretation of the BET model constants.

  • Fitting an isotherm regionally around an activity of relevance is sufficient for linking an isotherm to fluctuations, in contrast to the BET model, whose parameters are defined down at the zero sorbate activity limit (as will be shown in Results and Discussion).

  • The interfacial capacity, as the statistical thermodynamic generalization of the BET monolayer capacity, will be introduced, such that the BET analysis, which has been carried out for systems beyond the BET model assumptions, can be generalized to wider classes of sorption phenomena (in Results and Discussion).

Rigorous Statistical Thermodynamic Fluctuation Approach for Sorption

Fluctuation Theory Links an Isotherm to the Underlying Molecular Interactions

A statistical thermodynamic foundation is indispensable for overcoming the difficulties of BET surface area estimation identified in the Introduction (step I), instead of continuing to examine whether the BET model applies to a particular class of materials. As will be shown below, a statistical thermodynamic reinterpretation of the monolayer capacity and BET constant involves a particularly careful discussion on the low sorbate activity limit. Although our previous theory22 is valid at this limit (Supporting Information), a generalization is necessary to prove that we can focus safely on the amount of sorption, instead of the surface excess, even at this limit. Throughout this paper, we denote the sorbent as species 1 and the sorbate as species 2. We start from the generalized Gibbs isotherm, which is valid for any geometry, porosity, or granularity of the interface, regardless of molecular size and shape.21 Restricting our consideration to vapor–solid interfaces, we have shown previously that the difference between the ensemble-averaged (denoted by ⟨ ⟩) number of sorbates within the two subsystems of volume v, one at the interface, ⟨n2⟩, and another in the vapor (gas) and solid reference phases, ⟨n2g⟩ and ⟨n2⟩, is expressed as21

graphic file with name la2c00753_m002.jpg 1

where F is the free energy of the interface (Figure 1b). Equation 1 is applicable regardless of the interfacial geometry and porosity and is valid for adsorption and absorption alike.21,22 How the surface excess, Ns2 = ⟨n2⟩ – ⟨n2g⟩ – ⟨n2⟩, depends on the sorbate activity a2 can be characterized through its derivative

graphic file with name la2c00753_m003.jpg 2

in terms of the difference in sorbate–sorbate number correlations between the interface, ⟨δn2δn2⟩, and the vapor and solid reference systems, ⟨δn2gδn2⟩ and ⟨δn2sδn2⟩, with δn2n2 – ⟨n2⟩, δn2gn2 – ⟨n2g⟩, and δn2n2s – ⟨n2⟩ defined as the deviations from the mean sorbate numbers, respectively. (The background material for the derivation of eq 2 from eq 1 can be found, e.g., in p 129, eq 25.19 of ref (27)). How the isotherm depends on a2, according to eq 2, is governed by the excess number fluctuation.

Statistical Thermodynamic Isotherm Can Be Derived from Sorbate Number Fluctuations

Our next goal is to translate the BET monolayer capacity (the key quantity from which the BET surface area is calculated) into the language of rigorous statistical thermodynamics (step II in Introduction). To do so, we start from the following relationship which can be derived from eq 2 as the generalization of our previous paper,22 as

graphic file with name la2c00753_m004.jpg 3

Here, the sorbate excess number around a probe sorbate, N22, together with the corresponding quantities for the reference states (N22g and N22) have been introduced and defined as21,22

graphic file with name la2c00753_m005.jpg 4

(In deriving eq 3, the number–number correlations appearing from differentiating the numbers using eq 2 are replaced via eq 4 by the excess numbers.) The excess number is used universally in solutions,2830 interfaces,2123 surfactants,31 nanoparticles,32 and confined systems.33 The utility of eq 3 can best be seen in its following integrated form

graphic file with name la2c00753_m006.jpg 5

where A0 is a constant of integration (whose physical interpretation will be clarified below). Introducing the Maclaurin expansion of eq 3

graphic file with name la2c00753_m007.jpg 6

and combining it with eq 5 yields the following general isotherm (Figure 1c)

graphic file with name la2c00753_m008.jpg 7

Equation 7 is our statistical thermodynamic isotherm. Our previous theory21,22 results from ⟨n2⟩ – ⟨n2g⟩ – ⟨n2⟩ ≃ ⟨n2⟩ as shown in the Supporting Information. We will later demonstrate that eq 7 contains the BET model as its special case. Here, we show that the parameters have a clear physical meaning. First, we will establish how A0 is related to sorbate–surface interaction at the a2 → 0 limit (Figure 1c). This can be achieved by the relationship between a2 and the gas-phase density, c2g, via a2 = c2/c2o, with c2 being the vapor concentration in the saturated vapor through which A0–1 can be related to the surface–sorbate (or sorbent–sorbate) Kirkwood–Buff integral, Gs2, as22

graphic file with name la2c00753_m009.jpg 8

with the subscript denoting the a2 → 0 limit. Here, a positive surface–sorbate (or sorbent–sorbate) Kirkwood–Buff integral signifies the accumulation of sorbates at the interface compared to the vapor phase, whereas the negative value signifies their depletion at the interface. (The convergence of A0 will be shown by its correspondence to the BET parameters in the next paragraph, as well as a careful discussion on the limiting behavior in the Supporting Information.) Second, the parameter B0 is linked to the excess sorbate–sorbate number fluctuation at the a2 → 0 limit, as can be seen straightway from eq 6

graphic file with name la2c00753_m010.jpg 9

We emphasize that the sorbate–sorbate number fluctuation here already incorporates the influence by the presence of the interface (sorbent) because the sorbent has already been incorporated in carrying out the ensemble averaging in calculating ⟨n2⟩ and N22 (Figure 1c). In our discussion below, the statistical thermodynamic interpretations of the coefficients A0 and B0 will play a central role in clarifying the physical meaning of the BET model (Figure 1c). Although C0 is important for describing some limitations of the BET model, the expression for the coefficient C0 is complex, involving the sorbate triplet correlation as shown before22 and is not discussed further in this paper.

Interpreting the BET Model from the Statistical Thermodynamic Fluctuation Theory

Based on our generalized theory of sorption which is capable of describing the zero sorbate limit, here we show that the statistical thermodynamic isotherm (eq 7) has the mathematical form (i.e., the quadratic function of a2 in the denominator and a2 in the numerator) that contains the Langmuir,34 BET,6 and GAB1719 models as its special cases.22 This makes it possible to translate the “monolayer capacity” nm and “the BET constant” CB of the BET model (Figure 1a) into statistical thermodynamics (Figure 1b,c, step II in Introduction). The BET model has the following functional form:

graphic file with name la2c00753_m011.jpg 10a

Comparing eqs 7 and 10a leads to the following correspondence between the BET parameters and statistical thermodynamics

graphic file with name la2c00753_m012.jpg 10b

Or equivalently

graphic file with name la2c00753_m013.jpg 10c

Thus, the BET model parameters have been given a statistical thermodynamic interpretation by eq 10c, in combination with eqs 8 and 9. Based on this new interpretation, we will later clarify what the BET “monolayer capacity” signifies in the language of statistical thermodynamics (see Results and Discussion).

Regional Isotherm Fitting Around an Activity of Relevance is Sufficient for Linking an Isotherm to Fluctuations

So far, we have compared the BET model (eq 10a) with the statistical thermodynamic isotherm (eq 7) over the entire range of activity (a2). However, the protocol for the BET surface area calculation involves the identification of the a2 range in which the BET model fits the experimental isotherm data.9 Such a fitting region is to be found typically between a2 = 0.05 and 0.30, with the applicability of BET evidenced by the linearity of the BET plot.9 Hence, it is necessary to adapt our theory to regional isotherm fitting; that is, fitting over a small region of a2 around a reference (a2 = ar) instead of the global fit over all a2. To do so, the Maclaurin expansion in eq 6 is modified as

graphic file with name la2c00753_m014.jpg 11a

and the integration of eq 5 is changed to

graphic file with name la2c00753_m015.jpg 11b

with the constants Ar, Br, and Cr defined at a2 = ar. Ar is now linked to the surface–sorbate Kirkwood–Buff integral at a2 = ar

graphic file with name la2c00753_m016.jpg 11c

and Br is related to the sorbate number fluctuations at a2 = ar as

graphic file with name la2c00753_m017.jpg 11d

Also, Cr involves ternary number correlations. Defining the isotherm parameters regionally at a2 = ar will help overcome some of the historical difficulties surrounding the BET analysis of isotherms (Results and Discussion). The application of this approach will be simplified in the next paragraph.

Interfacial Capacity as the Statistical Thermodynamic Generalization of the BET Monolayer Capacity

The BET monolayer capacity is a quantity defined under the assumptions of the BET model. Our aim here is to define a statistical thermodynamic quantity, the “interfacial capacity”, as a generalization of the BET monolayer capacity and independent of the BET model assumptions. The key to generalization comes from the statistical thermodynamic translation of the BET model parameters (eqs 10b and 10c) and the IUPAC technical report (“[i]t is now generally agreed that the value of [CB] rather gives a useful indication of the shape of the isotherm in the BET range. Thus, if the value of [CB] is at least ∼80, the knee of the isotherm is sharp”10), supported also by the NIST recommendation which expresses that “[t]o obtain a reliable value of nm, it is necessary that the knee of the isotherm be fairly sharp (i.e., the BET constant [CB] is not less than about 100)”.35 Therefore, we can consider CB to be large. Under this condition, a combination of eqs 9 and 10b leads to the following relationship

graphic file with name la2c00753_m018.jpg 12a

Equation 12a can be considered as a special case (ar → 0) of the “interfacial capacity” defined as

graphic file with name la2c00753_m019.jpg 12b

which is valid both for the regional isotherm around a2 = ar as well as the global isotherm (ar → 0). Equation 12b is the statistical thermodynamic generalization of the monolayer capacity. Using eq 3, eq 12b can be rewritten as

graphic file with name la2c00753_m020.jpg 12c

Equation 12c allows nI to be calculated from any fitting equation. A practical approach is to apply eq 6 instead of eq 11a to carry out regional isotherm fitting within a range of finite a2. Combining eq 6 with eq 12c, we obtain the following simple expression

graphic file with name la2c00753_m021.jpg 12d

In addition to our isotherm (eq 7), other isotherm models can also be used with eq 12c. The physical meaning of nI will be presented in the next section. Thus, we have introduced the “interfacial capacity”, nI, as a statistical thermodynamic generalization of the BET monolayer capacity nm. As will be shown in the next section, nI will play an important role in understanding interfacial filling.

Results and Discussion

Overview

The statistical thermodynamic isotherm will replace the BET model as its model-free generalization.

  • Complications due to the BET model assumptions (Figure 1a) will be eliminated, leading to an easier fitting of isotherm data using the statistical thermodynamic isotherm (Figure 1c) without the need for the consistency criteria.

  • A new view of sorption will be established based on sorbate–sorbate exclusion, which has been neglected by the BET model.

Based on the demonstrated ease of fitting and interpretation of the statistical thermodynamic isotherm, the BET analysis will be generalized in the framework of the statistical thermodynamic fluctuation theory.

  • Problems with the BET monolayer coverage will be identified as being defined inadvertently at zero sorbate activity rather than at full interfacial coverage.

  • Interfacial coverage and filling will be redefined statistical thermodynamically as the point of strongest sorbate–sorbate exclusion (Point M).

  • Probing interfacial coverage and sorbate packing at Point M will lead to a statistical thermodynamic redefinition of the monolayer–multilayer behavior in adsorption.

This section concludes with a practical summary, a statistical thermodynamic guideline for surface area estimation.

Fitting Experimental Isotherms Can Be Facilitated by Removing the Restrictive BET Model Assumptions

BET Model is a Restricted Case of the Fluctuation Theory

The BET surface area is defined as the product of the BET monolayer capacity (nm) and the cross-sectional surface (σ2).9,10 We first focus on the problems associated with the evaluation of nm from the experimental isotherm using the BET model. As a first step, we consider an idealized case scenario in which the adsorption isotherm obeys the BET model for the entire a2 range. As the first step, we show that the BET plot is a restricted case of our statistical thermodynamic isotherm (eq 7), which can be rewritten as

graphic file with name la2c00753_m022.jpg 13

We emphasize that the three parameters (A0, B0, and C0 with a statistical thermodynamic interpretation in the Theory section) refer to the dilute sorbate limit, a2 → 0, and are related to the BET parameters via eqs 10b and 10c. In the BET model, the three parameters are not independent; eq 10b reveals the following constraint for the BET model

graphic file with name la2c00753_m023.jpg 14a

through which eq 13 can be rewritten as

graphic file with name la2c00753_m024.jpg 14b

which is identical to the well-known BET plot shown indeed in Figure 2b.9,10 To summarize, the BET plot (eq 14b) contains only two independent parameters compared to three (eq 13) due to the BET model assumption (eq 14a).

Force-Fitting the BET Model to Systems beyond the BET Assumptions is the Cause of Difficulties

The BET and Langmuir are highly idealized models. Experimental isotherms often deviate from these models, which poses difficulties to the BET analysis, as discussed in the Introduction. Such a deviation can be captured insightfully by our statistical thermodynamic isotherm (eq 7), which does not involve the constraints imposed by the BET (eq 14a) or Langmuir (C0 = 0) models. To demonstrate this systematically, we have chosen the following systems as examples.

  • I

    The adsorption isotherms of water and nitrogen on a Portland cement paste (Figure 3a) measured by Maruyama et al.36,37

  • II

    The adsorption of argon and nitrogen on zeolite 13X (Figures 4a and 5a) measured by Pini38,39 and chosen by Rouquerol et al.3 to illustrate the difficulties of applying the BET analysis to microporous systems.9,10

Carrying out the BET analysis via eq 14b (Figures 3b, 4b, and 5b) and determining the parameters for the statistical thermodynamic isotherm via eq 13 (Figures 3c, 4c, and 5c) reveal their varying degrees of closeness to the BET and Langmuir models.

Figure 3.

Figure 3

Adsorption of water at 293 K (blue circles) and nitrogen at 77.4 K (black squares) on a Portland cement paste using the data published by Maruyama et al.36,37 (a) Adsorption isotherms. (b) BET plot (eq 14b), leading to CB = 17.2 and nm = 2.86 mmol/g for water and CB = 80.6 and nm = 1.09 mmol/g for nitrogen, with the resultant BET surface areas from nm (196 m2/g for water, 106 m2/g for nitrogen) consistent with Maruyama et al.36,37 (c) Inline graphic plot (eq 13) with the fitting parameters listed in Table 1.

Figure 4.

Figure 4

Adsorption of argon on crystalline (red squares) and pelleted (black circles) zeolite 13X using the data published by Pini at 87 K.38 (a) Adsorption isotherms. (b) BET plot (eq 14b). Dotted lines: linear fit based on data between a2 = 0.2 and 0.3 with the unphysical intercepts of Inline graphic (red) and −7.56 (black), respectively; dashed lines: linear fit based on the data between a2 = 0.05 and 0.1, with the unphysical intercepts of Inline graphic (red) and −0.0034 (black). (c) Inline graphic plot (eq 13) with the fitting parameters listed in Table 1. The dashed and dotted lines were calculated under the BET (C0 = 2(A0B0)) and Langmuir (C0 = 0) constraints.

Figure 5.

Figure 5

Adsorption of nitrogen on crystalline (red squares) and pelleted (black circles) zeolite 13X using the data published by Pini at 77 K.38 (a) Adsorption isotherms. (b) BET plot (eq 14b). Solid lines: linear fit based on data between a2 = 0.05 and 0.3 with the unphysical intercepts of Inline graphic (red) and −3.05 (black), respectively. (c) Inline graphic plot (eq 13) with the fitting parameters listed in Table 1. The dashed and dotted lines were calculated under the BET (C0 = 2(A0B0)) and Langmuir (C0 = 0) constraints.

  • I

    Both nitrogen and water isotherms for Portland cement can be modeled by the BET model, as evidenced by the linearity of the BET plot (Figure 3b) and by the value of C0 being not too far from the BET constraint, that is, 2(A0B0) (eq 14a) as shown in Table 1.

  • II

    The BET analysis for zeolite (Figures 4b and 5b) leads to difficulties (as will be discussed below) because the isotherms do not satisfy the condition for the BET model, C0 = 2(A0B0). Judging from the value of C0 (Table 1), the argon adsorption on pelleted samples is neither BET-like nor Langmuir-like. The rest of the isotherms are close to the Langmuir model yet not strictly so because of C0 ≠ 0 (Table 1).

Given that the BET model is satisfied to a varying degree by the real isotherms, how can we establish a method of surface area estimation that can be used universally instead of force-fitting the BET model to the systems that deviate from it?

Table 1. Parameters for the Statistical Thermodynamic Isotherm and a Test of Closeness to the BET (C0 = 2(A0B0)) and Langmuir (C0 = 0) Modelsa.
sorbate–sorbent fitting a2 range A0 g/mmol B0 g/mmol C0 g/mmol 2(A0 – B0) g/mmol
  eq 13 eq 13 eq 13 eq 13 eq 14a
water/Portland cementb 0.04–0.3 1.78 × 10–2 3.43 × 10–1 8.40 × 10–1 7.22 × 10–1
N2/Portland cementb 0–0.25 4.00 × 10–3 1.02 × 100 2.64 × 100 2.04 × 100
Ar/crystalline zeolite 13Xc 0–0.4 1.04 × 10–4 1.03 × 10–1 3.46 × 10–2 2.06 × 10–1
Ar/crystalline zeolite 13Xc 0.01–0.15 1.33 × 10–4 1.04 × 10–1 4.38 × 10–2 2.08 × 10–1
Ar/pelleted zeolite 13Xc 0–0.4 1.51 × 10–4 1.36 × 10–1 1.16 × 10–1 2.73 × 10–1
Ar/pelleted zeolite 13Xc 0.01–0.15 2.06 × 10–4 1.40 × 10–1 1.80 × 10–1 2.81 × 10–1
N2/crystalline zeolite 13Xc 0–0.4 1.17 × 10–5 1.09 × 10–1 1.01 × 10–2 2.18 × 10–1
N2/pelleted zeolite 13Xc 0–0.4 1.64 × 10–5 1.35 × 10–1 4.01 × 10–2 2.70 × 10–1
a

All R2 values were above 0.9987.

b

Data reported by Maruyama et al.36,37

c

Data reported by Pini.38

Fundamental Assumptions of the BET Model May be Broken

The first step of surface area determination by BET is to identify the linear region of the BET plot (eq 14b). (Such a process is unnecessary for an isotherm which strictly obeys the BET model, Figure 2b.) The IUPAC guideline advises the linear region to be chosen usually between a2 = 0.05 and 0.30.9 The Portland cement isotherms exhibited good linearity in this a2 range (Figure 3b). For zeolites, the a2 regions within this guideline, 0.05 ≤ a2 ≤ 0.1 and 0.20 ≤ a2 ≤ 0.3 for Figure 4b and 0.05 ≤ a2 ≤ 0.3 for Figure 5b, gave negative values for the intercept (Inline graphic in eq 14b) contradictory to the positive CB and nm assumed by the BET model. This is because, outside the range of very small a2 (<0.05), these isotherms violate the consistency criteria listed in Introduction (Table 2). However, how can we analyze isotherms in a simpler manner without the laborious check against the four consistency criteria?

Table 2. Determination of Argon and Nitrogen BET Surface Areas of Zeolite 13X Cross-Validated with the Consistency Criteria.
sorbate–sorbent fitting rangeb data pts CB nmc BET surface aread (1 – a2) ⟨n2⟩ increases until a2= a2 for nm
graphic file with name la2c00753_m051.jpg
Ar/crystal 0.0003–0.04 21 2.51×103 9.10 775 4.27 × 10–2 1.92 × 10–2 1.96 × 10–2
Ar/pellet 0–0.05 22 1.49×103 6.85 585 7.32 × 10–2 2.46 × 10–2 2.52 × 10–2
N2/crystal 0–0.01 20 7.09×104 8.82 859 1.09 × 10–2 3.73 × 10–2 3.74 × 10–3
N2/pellet 0–0.04 19 4.71×104 7.07 689 9.74 × 10–3 4.56 × 10–3 4.59 × 10–3
criteriona     A     B C D
the values must be     positive     above the fitting range within the fitting range close to the left column
a

See the list in the Introduction.

b

R2 values were above 0.9996.

c

Units in mmol/g.

d

Units in m2/g.

Removing the BET Restrictions via Statistical Thermodynamics Facilitates Fitting

The difficulty in the BET analysis for zeolite isotherms comes from the restrictive assumption of the BET model (eq 14a) that is not satisfied (Table 1). Therefore, eq 13, free of the BET assumptions, can fit the experimental isotherm over a range of a2 between a2 = 0 and 0.4 (Figures 4c and 5c), much wider than the linear regions of the BET plot (Table 2). A straightforward analysis is afforded by the general statistical thermodynamic formula without any constraints on its parameters (eq 13).

Sorbate–Sorbate Exclusion is the Key to the Statistical Thermodynamic Understanding of Isotherms

Our Strategy

Due to the limitations of the BET model, a new theoretical foundation is necessary for surface area estimation. To achieve this goal, our strategy is to fulfill what the BET analysis has aimed to achieve without the restrictions of the BET model. To this end, we will reformulate the key concepts of the BET model (such as the monolayer capacity, the BET constant, and monolayer filling) in the framework of the statistical thermodynamic fluctuation theory based on the correspondence that we have already established (eqs 10b and 10c).

Presence of the Interface Affects Sorbate–Sorbate Distribution

We have seen the importance of the sorbate–sorbate excess number N22 in the Theory section. N22 is related to the (log–log) gradient of the isotherm as21,22

graphic file with name la2c00753_m026.jpg 15a

which is a simplified version of eq 2 applicable to common interfaces. Understanding the effect of the interface on sorbate–sorbate interaction can be facilitated by introducing the sorbate–sorbate Kirkwood–Buff integral, G22, as21,28,30,40

graphic file with name la2c00753_m027.jpg 15b

where v is the volume of the interfacial layer (e.g., for a planar, monolayer surface, v is simply the product of the monolayer thickness and the interfacial surface area), and c2 = ⟨n2⟩/v is the concentration of sorbates at the interface. The sign of G22 is an important signature of sorbate–sorbate interaction; a positive G22 represents a net sorbate–sorbate attraction, whereas a negative G22 signifies a net exclusion of sorbates from a probe sorbate.21,28,30,40 As will be shown below, G22 is negative for adsorption obeying the BET model. This is in contrast to the positive sign of G22g, that is, the sorbate–sorbate Kirkwood–Buff integral of the vapor phase evaluated from the experimental virial coefficients4143 (Supporting Information), showing that the presence of the interface influences the sorbate–sorbate distribution, making it different from the vapor phase. In this manner, how the interface (or sorbent) affects the sorbate–sorbate interaction can be captured quantitatively by the Kirkwood–Buff integral.

Sorbate–Sorbate Exclusion Determines the BET Constant and Interfacial Capacity

Here, we show statistical thermodynamically that the BET monolayer capacity and the BET constant can only be positive under sorbate–sorbate exclusion, which seems surprising from the common understanding of the BET theory. First, the BET monolayer capacity nm (eq 12a) is the ar → 0 limit of the interfacial capacity (eq 12b), which can be simplified as

graphic file with name la2c00753_m028.jpg 16

For the monolayer capacity to be positive, as postulated by the BET model,3,9,10G22 at ar → 0 must be negative. This is underscored by the statistical thermodynamic expression of the BET constant simplified in combination of eqs 8, 9, 10c, and 11b as

graphic file with name la2c00753_m029.jpg 17

where c2o is the concentration of the saturated sorbate vapor, and K is the vapor-interface partition coefficient. For the BET constant to be positive (as has been assumed by the BET model), G22 must again be negative, which signifies sorbate–sorbate exclusion. We emphasize that a positive sign of −G22, which makes nI and CB positive, can be interpreted as the measure of volume that a probe molecule occupies at the interface. (Such an interpretation may be most intuitive for thick interfaces, verging onto a bulk liquid, where the positive −G22 signifies the volume occupied by a sorbate molecule according to the Kirkwood–Buff theory of liquids.40,44,45) Therefore, the positive −G22 as the measure of probe volume at the interface is the generalization of the bulk liquid argument. Such a statistical thermodynamic interpretation is in contrast with the conventional understanding that the BET constant “is exponentially related to the energy of monolayer adsorption.”10

Problems with the BET Monolayer Coverage

BET Parameters are Defined at the Dilute Sorbate Limit Far Away from the Monolayer Coverage

The goal of the BET analysis for surface area estimation is to probe “a complete monolayer of atoms or molecules in close-packed array”.8 However, both nm and CB correspond to the dilute sorbate limit (a2 → 0), as has been shown above (eqs 10b and 10c). This seemingly surprising conclusion can be supported also from a perspective based purely on the BET plot (eq 14b, Figures 4b and 5b). The monolayer capacity nm and the BET constant CB are evaluated from its gradient (Inline graphic) and intercept (Inline graphic), respectively. The intercept, by definition, is the value at a2 = 0. Therefore, against its claim of capturing monolayer coverage, the monolayer capacity in the BET model is inadvertently defined at the a2 → 0 limit far away from monolayer coverage.

Dilute Sorbate Limit May Be Hypothetical

Here, we demonstrate that the dilute sorbate limit does not correspond to the real sorption behavior at the same limit. (How adsorption at very low a2 can be measured experimentally4652 is summarized in the Supporting Information). Extrapolation requires a fitting function. However, even with the use of the general polynomial free of BET (eq 13), the extrapolation at a2 → 0 may still be different from the real system behavior at this limit. For example, at very low a2, a negative experimental gradient (positive B0) of the Inline graphic plot for argon (Figure 6) corresponds (via eq 9) to a positive sorbate–sorbate excess number opposite in sign from the extrapolated behavior. Thus, using the unreal a2 → 0 extrapolation is problematic for surface area estimation.

Figure 6.

Figure 6

The low a2 behavior of the argon adsorption on crystalline (red) and pelleted (black) zeolite 13X using the data published by Pini at 87 K.38 (a) Adsorption isotherms. (b) The BET plot (eq 14b) which exhibits a negative gradient at a2 → 0. (c) Inline graphic plot with the fitting equation (eq 13 with C0 = 0) using data between a2 = 4 × 10–4 and 1 × 10–3.

Overcoming the Problems with the BET Monolayer Capacity by Redefining Interfacial Coverage and Filling via Statistical Thermodynamics

Point M as the Completion of Interfacial Coverage

Our goal is to establish a reliable and facile alternative to BET analysis. The BET analysis has aimed, via nm, to quantify the amount of adsorption at the knee of the isotherm at which the completion of monolayer filling is assumed to take place.2,7,9,10 However, as discussed in the Introduction, since the precise location of the knee (or Point B) is unclear and becomes even more so as CB becomes smaller, the BET monolater capacity and the amount of adsorption at Point B may not be reliable quantitative measures. In addition, even though the consistency criteria helped eliminate unphysical results, they have complicated the BET analysis procedure; the root cause of the complication is trying to fit the BET model to the systems that break the BET model assumption (C0 ≠ 2(A0B0) (Table 1). To overcome these shortcomings, here, we introduce Point M, at which N22 takes a minimum, and calculate the amount of sorption at this point. (For an intuitive grasp of Point M, the reader may refer to our results in advance for the Portland cement (Figure 7) and zeolite 13X (Figure 8).) Combining eqs 7 and 15a under ⟨n2⟩ – ⟨n2g⟩ – ⟨n2⟩ ≃ ⟨n2⟩ (Supporting Information), we obtain

graphic file with name la2c00753_m033.jpg 18a

At Point M, (a2 = aM), Inline graphic must be satisfied, which leads to

Figure 7.

Figure 7

(a) Adsorption of water (blue circles) and nitrogen (black squares) on a Portland cement paste (Figure 3), with the indication of the respective amounts of adsorption at Point M, ⟨n2M at a2 = aM, calculated using eqs 18c and 18d. nm is the corresponding BET monolayer capacity determined in Table 2. (b) Excess numbers of sorbates around a probe sorbate, N22, calculated using eq 18a (with the parameters from Table 1) for water (blue circles) and nitrogen (black squares). Point M, where N22 is minimum, is calculated using eq 18c.

Figure 8.

Figure 8

(a) Adsorption of argon on crystalline (red squares) and pelleted (black circles) on zeolite 13X (Figure 4), with the indication of the respective amounts of adsorption at Point M, ⟨n2M at a2 = aM, calculated using eqs 18c and 18d. nm is the corresponding BET monolayer capacity determined in Table 2. (b) Excess numbers of sorbates around a probe sorbate, N22, calculated using eq 18a (with the parameters from Table 1) for crystalline (red squares) and pelleted (black circles) zeolite 13X. Point M, where N22 is minimum, is calculated using eq 18c.

graphic file with name la2c00753_m035.jpg 18b

Solving eq 18b under B0 < 0 for sorbate–sorbate exclusion,22 we obtain

graphic file with name la2c00753_m036.jpg 18c

Consequently, the amount of adsorption at Point M can be calculated using eqs 7 and 18b as

graphic file with name la2c00753_m037.jpg 18d

Restricting our result (eq 18d) to the BET model using eq 10b, we obtain the following expression for the amount of adsorption at Point M

graphic file with name la2c00753_m038.jpg 18e

The approximation at the final step is accurate for large CB. The location of aM can also be specified as

graphic file with name la2c00753_m039.jpg 18f

Equations 18e and 18f are significant; for large CB (as recommended by IUPAC), the monolayer capacity is equivalent to the amount of sorption at Point M for the BET model. Previously, Inline graphic was identified as the point at which the amount of sorption reaches the monolayer capacity, ⟨n2⟩ = nm.53 This point has made it to one of the consistency criteria (D) for the BET analysis (see Introduction).3,15 Note that aM and Inline graphic are close in values, with less than 12% difference for CB > 80, providing a statistical thermodynamic support for the consistency criterion D. However, beyond being the point at which ⟨n2⟩ = nm, the physical meaning of the latter has remained unknown, and its applicability has been limited within the BET analysis. In contrast, Point M can be defined for any isotherm.

Surface Area Estimation from the Adsorption at Point M

The location of Point M has been defined precisely for the BET model (eq 18f) and even for the statistical thermodynamic isotherm (eq 18c). Therefore, the amount of adsorption at Point M ⟨n2M is a viable alternative for the estimation of the monolayer capacity, nm. Indeed, ⟨n2M, calculated via eq 18d, agrees reasonably with the monolayer capacity calculated from the BET analysis (Table 3, which reports a comparison between the statistical thermodynamic surface area ⟨n2Mσm with the BET surface area nmσm, using the standard values of sorbate cross-sectional areas). Point M values can be calculated precisely by eq 18c, and their location around the knee can be inspected visually by Figures 7 and 8. The clarity in locating Point M contrasts with the inherent ambiguity of Point B.7 The clear physical picture underlying the definition of Point M (i.e., minimum N22) contrasts with the lack of interpretation of Inline graphic in the criterion D and its strict dependence on the BET model. Moreover, the interfacial capacity nI agrees with the amount of sorption at the knee only at a2 → 0 under the condition that adsorption obeys the BET model down to a2 → 0. Thus, we propose the amount of adsorption at Point M as the statistical thermodynamic alternative for the BET monolayer capacity.

Table 3. Surface Area Estimation via Statistical Thermodynamic Fluctuation Theory Using the Parameters (A0, B0, and C0) in Table 1.
sorbate–sorbent fitting a2 range aM n2M mmol/g (N22)M stat therm surface area (STSA) m2/g BET surface area m2/g (Table 2)
    eq 18c eq 18d eq 18a n2Mσmd nmσmd
water/Portland cementa 0.04–0.3 0.127 2.32 –0.55 160d 196e
N2/Portland cementa 0–0.25 0.048 0.96 –0.86 94d 106e
Ar/crystalline zeolite 13Xb 0–0.4 0.076 9.69 –0.97 829 789
Ar/crystalline zeolite 13Xb 0.01–0.15 0.075 9.63 –0.97 823 789
Ar/pelleted zeolite 13Xb 0–0.4 0.049 7.32 –0.96 626 585
Ar/pelleted zeolite 13Xb 0.01–0.15 0.045 7.10 –0.94 607 585
N2/crystalline zeolite 13Xb,c 0–0.4 0.048 9.17 –0.99 895 860
N2/pelleted zeolite 13Xb,c 0–0.4 0.028 7.40 –0.99 722 690
a

Data reported by Maruyama et al.36,37

b

Data reported by Pini.38

c

A narrower fitting range was not feasible due to the sparseness of data around aM

d

We have used the cross-sectional area, σm, for argon (0.142 nm2) and N2 (0.162 nm2) taken from the IUPAC recommendations and the one for water (0.114 nm2) taken from Odler.12

e

Compared to 196 and 113 m2/g by Aili and Maruyama.37

Advantage of Statistical Thermodynamic Surface Area Estimation over the BET Model

Point M can be identified simply by fitting the statistical thermodynamic isotherm (eq 10a) around the knee (Figures 7 and 8), without any need for the restrictive BET assumptions, the cumbersome consistency criteria, and the problematic extrapolation to a2 → 0. Note that a very shallow minimum at Point M for the crystalline zeolite (Figure 8) does not pose any problem because N22 ≃ −1 means that the isotherm has a near-zero gradient (N22 + 1 ≃ 0); hence, a small error in positioning Point M does not lead to inaccuracies in the amount of adsorption at that point. Point M, defined as the minimum sorbate–sorbate excess number N22, has a clear microscopic interpretation. ⟨n2M is also defined clearly as the net excess sorbate–surface distribution function21,22 at this point. Unlike the BET model constants, these distribution functions can be calculated directly from molecular simulation, thereby allowing a direct comparison between simulated and experimental values. Thus, a statistical thermodynamic identification of Point M removes the need for the BET model altogether in surface area estimation.

Probing Interfacial Coverage and Sorbate Packing Statistical Thermodynamically at Point M

Sorbate–Sorbate Interaction as the Measure for Knee Sharpness

In the BET analysis, the BET constant CB, which determines the shape of an isotherm, is used as a measure for the sharpness of the knee and therefore as evidence for monolayer completion as a prerequisite for surface area determination.9,10 IUPAC recommends the BET constant be larger than 80.9,10 This recommendation, however, cannot be used for isotherms that do not obey the BET model. Therefore, a new quantitative guideline, independent of sorption models, is necessary. To this end, a relationship between N22 at Point M and CB will be helpful, which can be derived by combining eqs 10b, 18a, 18e, and 18f as

graphic file with name la2c00753_m043.jpg 19

Using eq 19, a one-to-one correspondence between CB and (N22)M can be established for the BET model (Figure 9). The IUPAC recommendation that CB must be larger than 80 is translated as N22 should be below (i.e., more negative than) −0.78. This criterion also means ⟨n2M/(nI)M > 0.78, meaning that the amount of sorption at Point M is more than 78% of the interfacial capacity. This new criterion, formulated via N22, can be applied to any isotherm. The meaning of this criterion will be clarified in the next two paragraphs.

Figure 9.

Figure 9

Relationship between the BET constant, CB, and the excess number of sorbates around a probe sorbate, (N22)M, at Point M plotted using eq 19 derived for the BET model. The IUPAC recommendation that CB should be larger than 80 for the clarity of the knee corresponds to N22 below −0.78. The recommendation based on N22 can be applied beyond the boundary of the BET model.

Probing the Close Packing of an Interface via the Sorbate–Sorbate Excess Number

To understand the physical meaning of Point M, let us first consider a case in which the gradient of an isotherm is very small at Point M, namely, N22 ≃ −1. Such a condition is satisfied by the nitrogen and argon adsorption on zeolite 13X (Figure 8) but is different from the Portland cement isotherms (Figure 7, Table 3). N22 ≃ −1 at Point M is equivalent to

  • a

    a very small sorbate number variance, ⟨δn2δn2⟩ ≃ 0, at Point M, according to eq 4;

  • b

    approximately one sorbate molecule in total being excluded around a probe sorbate, N22 ≃ −1 at Point M, according to eq 4; and

  • c

    the amount of adsorption is close to the interfacial capacity at Point M, (nI)M ≃ ⟨n2M, according to eq 16.

A physical picture of Point M adsorption emerges from (a)–(c) for this case (Figure 8). The interface contains a well-defined number of sorbates because the number fluctuation is small (a). The sorbate molecules are uniformly distributed in the interface because introducing a probe sorbate excludes one sorbate molecule around it (b). Under such a close and uniform packing, the amount of sorption at Point M is close to the interfacial capacity (c). (At the limit of a very thick interface or a bulk sorptive liquid, (a)–(c) can be considered as the conditions for very small compressibility). Therefore, (a)–(c) are the statistical thermodynamic characterizations of very close sorbate packing, most probably due to filling up micropores (which is likely to be the case for zeolite 13X).23

Sorbate–Sorbate Excess Number May Be a Measure of Monolayer–Multilayer Overlap

Unlike the idealized case in the previous paragraph, the minimum of N22 is usually above −1 for BET-like systems (Table 3). The existence of a sharp knee corresponds to N22 below −0.78 (Figure 9). According to IUPAC, the value of CB being less than 80 (or, more generally, N22 above −0.78) is “an indication of a significant amount of overlap of monolayer coverage and the onset of multilayer adsorption”.10 This is the case for water adsorption on Portland cement, while nitrogen adsorption behaves closer to the previous paragraph (Figure 7). Compared to N22 ≃ −1 at Point M, this case shows that

  • a

    the sorbate number variance, ⟨δn2δn2⟩, is larger (eq 4);

  • b

    when a probe sorbate is placed, less than one sorbate is excluded (eq 4); and

  • c

    the amount of adsorption is smaller than the interfacial capacity at Point M, (nI)M > ⟨n2M (eq 16).

Thus, the interface is characterized by the less definite number of sorbates (a) and inhomogeneity in the distribution of sorbates; that is, the presence of a probe molecule (whose center of mass is at rest) makes its vicinity deviate from the sorbate distribution (b). Due to the inhomogeneity and fluctuation at the interface, the amount of adsorption does not reach the interfacial capacity at Point M (c). (Using, as before, the limit of a very thick interface or a bulk sorptive liquid, (a)–(c) correspond to higher compressibility). Such an interfacial behavior is reminiscent of a “significant overlap of monolayer coverage and the onset of multilayer adsorption”10 as viewed from the fluctuation theory.

Monolayer Coverage May Take Place between the Two Extremes

While small CB is the sign of monolayer–multilayer overlap, “[a] high value of [CB] (say, >∼150) is generally associated with either adsorption on high-energy surface sites or the filling of narrow micropores.”10 The recommended values of CB between 80 and 150 correspond to the range of N22 at Point M between −0.78 and −0.84. The BET-based IUPAC guideline was translated to the more universal language of statistical thermodynamics, applicable beyond the bounds of the BET model. However, more investigations are necessary to specify the range of N22 for monolayer coverage with sufficient clarity for surface area estimation. We have shown that the monolayer–multilayer adsorption mechanism may be operative between the two extremes.

Quality of Surface Area Estimation Depends on the Probe Used

The significant difference in surface area between water and nitrogen sorbate probes has been recognized for a long time,12 which is true also for the Portland cement (Table 3). However, the quality of surface area determination depends on the probes used. We first note that the minimum N22 for water is −0.55, while that for nitrogen is −0.86 (Table 3). A larger N22 means a steeper isotherm gradient; a stronger water–water interaction helps adsorb more water onto the interface. However, according to the correspondence between N22 and CB (Figure 9), water fails the IUPAC recommendation of CB > 80 while nitrogen satisfies it. Microscopically, ⟨n2M = 0.55(nI)M (eq 16) means that the amount of water adsorption at Point M is only half of its interfacial capacity. Based on the previous paragraph, water adsorption exhibits a significant overlap between monolayer coverage and multilayer adsorption. Consequently, nitrogen seems to be a more appropriate probe than water for surface area estimation in this particular system.

Statistical Thermodynamic Guideline for Surface Area Estimation

Procedure

Here, we summarize the statistical thermodynamic analysis in terms of the following list of procedures for surface area estimation:

  • 1

    Fit an experimental isotherm around its knee using eq 13 (Figures 3c, 4c, and 5c, and Table 1).

  • 2

    Calculate the location of Point M (aM) using eq 18c and the amount of adsorption at Point M (⟨n2M) eq 18d (Table 3).

  • 3

    Estimate the surface area by multiplying ⟨n2M by the probe molecule’s cross-sectional area σm (Table 3). This can be called the statistical thermodynamic surface area (STSA) as an alternative for the BET surface area.

Note that a2 and ⟨n2⟩ correspond directly to p/p0 and n of the IUPAC notation, respectively. Hence, aM and ⟨n2M are simply p/p0 and n at Point M, respectively. Here are the considerations for a sense check:

  • the location of aM and ⟨n2M are roughly around the knee of an isotherm (Figure 7a and 8a);

  • the calculated aM via eq 18c is indeed at the minimum of N22 (Figures 7b and 8b);

  • N22 at Point M is between −0.78 and −0.84 for a sign of monolayer coverage (Figures 7b, 8b, and 9). The value of N22 should be quoted with STSA.

This range of N22 is the statistical thermodynamic translation of the IUPAC guideline10 for CB to be between 80 and 150 for the monolayer–multilayer mechanism, which requires further work for clarification.

Evaluating the Underlying Assumptions via Simulation

The above procedure for surface area estimation still contains the following assumptions inherited from the BET analysis:

  • (a)

    The interface can be approximated as a planar monolayer.

  • (b)

    The standard value of the probe’s cross-sectional area is valid.

Fortunately, a key attribute of the approach here is that the above assumptions can be examined via classic molecular dynamics or Monte Carlo simulations that allow the evaluation of these key statistical thermodynamic quantities. (a) If the interface is a monolayer, the sorbate–surface correlation function has a sharp first peak and further peaks are negligibly small. For an interface that cannot be considered planar or monolayer (such as microporous materials like zeolite), reporting the Point M capacity instead of the surface area may be more realistic. (b) The effective molecular size of sorbates can be evaluated using the sorbate–sorbate distribution function. Thus, the macroscopic (the isotherm) and microscopic (i.e., molecular dynamics or Monte Carlo simulations) pictures of sorption can be linked and cross-validated.

Monolayer Versus Pore Filling

Extensive comparisons with simulation have revealed recently that the BET approach overestimates the surface area due to the contributions from pore filling14 and that distinguishing pore filling and monolayer filling is crucial for a reliable surface area determination.15 Addressing this difficult question requires further work. However, we would like to point out, based on our previous work on adsorption on porous materials,21,23,24 that N22 may still play a crucial role in connecting the gradient of an isotherm to the number of sorbates that sorb cooperatively. N22 changes with a2 (Figures 7b and 8b) and plays a central role in understanding how a macroscopic isotherm is composed of different sorption processes.

Conclusions

Difficulties have persisted in surface area estimation using the BET analysis of an isotherm. The present paper has identified the causes of the difficulties and demonstrated how they can be overcome. Difficulties have arisen from

  • i

    trying to fit the BET model to the isotherms that break its basic assumptions; and

  • ii

    ambiguous and unclear physical meanings of the BET constant and the monolayer capacity

The introduction of the consistency criteria helped eliminate the unphysical solutions in (i) but has perpetuated (ii) by making what looks like a straightforward linear plot (the BET plot) more complicated to use. The statistical thermodynamic fluctuation theory, due to its model-free nature, has

  • i

    shown that the statistical thermodynamic isotherm, whose special and restricted case is the BET model, removes the need for force-fitting the BET model to sorption data; and

  • ii

    translated the objectives of the BET analysis into the language of the fluctuation theory.

We have removed the need for the BET model to carry out surface area estimation.

Our new, alternative approach is the generalization of the BET analysis and can be carried out without its restrictive assumptions or a force-adaptation of the BET model to reality. The key ideas are

  • I

    the excess number N22, a measure of sorbate–sorbate interaction at the interface, as central to interfacial coverage;

  • II

    Point M, at which N22 takes the minimum value, as the precise location of interfacial coverage; and

  • III

    adsorption at Point M replaces the monolayer capacity for calculating the surface area.

This new procedure for the calculation of the statistical thermodynamic surface area (STSA) can be carried out without being restricted to an isotherm model and without the consistency criteria necessitated by using a model beyond its applicability. In our statistical thermodynamic generalization of BET-based approaches, the excess number, N22, as a measure of sorbate–sorbate interaction at the interface, will play a central role

  • as a replacement of the BET constant, representing the clarity of the knee and the applicability of the monolayer coverage;

  • in linking the macroscopic measurement (isotherms) to microscopic (simulation) measurement, to clarify, for example, whether the interfacial filling is monolayer-like, pore-filling-like, or with a significant monolayer–multilayer overlap; and

  • as a measure of sorption cooperativity, which is especially important for porous systems.

Thus, the problems of the BET analysis have been overcome by the clarity, generality, and applicability afforded by model-free statistical thermodynamics. This was brought about by a statistical thermodynamic generalization of the BET approach. However, this does not mean that our new general theory eliminates the difficulties posed by the monolayer–multilayer overlap or the ambiguity in distinguishing between monolayer coverage and pore filling. What we have achieved is to establish the general statistical thermodynamic measures for interfacial filling that do not depend on a restricted isotherm model. To address these questions, a systematic comparison with computer simulation is indispensable in conjunction with our new approach. The extension of our approach includes an examination of other approaches to surface area estimation based on different adsorption models and to clarify how the difference between the monolayer and pore-filling behaviors manifests in isotherms.

Acknowledgments

We are grateful to Steven Abbott for his careful and critical reading of our article at many stages and to Kaja Harton and Olivia Dalby for valuable discussions. We thank Abudushalamu Aili and Ippei Maruyama for sending us the adsorption data on Portland cement. N.M. is grateful to the Grant-in-Aid for Scientific Research (no. JP19H04206) from the Japan Society for the Promotion of Science and by the Elements Strategy Initiative for Catalysts and Batteries (no. JPMXP0112101003) and the Fugaku Supercomputing Project (no. JPMXP1020200308) from the Ministry of Education, Culture, Sports, Science, and Technology.

Supporting Information Available

The Supporting Information is available free of charge at https://pubs.acs.org/doi/10.1021/acs.langmuir.2c00753.

  • Negligibility of the vapor reference system; interfacial versus vapor contributions to the surface excess; vapor-interface partition function; and measuring sorption at an infinitely dilute sorbate limit (PDF)

The authors declare no competing financial interest.

Supplementary Material

la2c00753_si_001.pdf (272.7KB, pdf)

References

  1. Sing K. S. W.; Williams R. T. Empirical Procedures for the Analysis of Physisorption Isotherms. Adsorpt. Sci. Technol. 2005, 23, 839–853. 10.1260/026361705777641990. [DOI] [Google Scholar]
  2. Rouquerol F.; Rouquerol J.; Sing K. S. W.. Adsorption by Powders and Porous Solids, 2nd ed.; Elsevier: Amsterdam, 2003; pp 237–438. [Google Scholar]
  3. Rouquerol J.; Llewellyn P.; Rouquerol F. Is the BET Equation Applicable to Microporous Adsorbents?. Stud. Surf. Sci. Catal. 2007, 160, 49–56. 10.1016/s0167-2991(07)80008-5. [DOI] [Google Scholar]
  4. Adamson A. W.; Gast A. P.. Physical Chemistry of Surfaces; Wiley: New York, 1997; pp 599–684. [Google Scholar]
  5. Butt H.-J.; Graf K.; Kappl M.. Physics and Chemistry of Interfaces; Wiley-VCH: Weinheim, 2013; pp 229–265. [Google Scholar]
  6. Brunauer S.; Emmett P. H.; Teller E. Adsorption of Gases in Multimolecular Layers. J. Am. Chem. Soc. 1938, 60, 309–319. 10.1021/ja01269a023. [DOI] [Google Scholar]
  7. Gregg S.; Sing K. S. W.. Adsorption, Surface Area, and Porosity; Academic Press: London, 1982; pp 111–194. [Google Scholar]
  8. McNaught A. D.; Wilkinson A.. IUPAC Compendium of Chemical Terminology. The Gold Book, 2nd ed.; International Union of Pure and Applied Chemistry: Zürich, 2014; p 961. [Google Scholar]
  9. Sing K. S. W.; Everett D. H.; Haul R. A. W.; Moscou L.; Pierotti R. A.; Rouquerol J.; Siemieniewska T. Reporting Physisorption Data for Gas/Solid Systems with Special Reference to the Determination of Surface Area and Porosity. Pure Appl. Chem. 1985, 57, 603–619. 10.1351/pac198557040603. [DOI] [Google Scholar]
  10. Thommes M.; Kaneko K.; Neimark A. V.; Olivier J. P.; Rodriguez-Reinoso F.; Rouquerol J.; Sing K. S. W. Physisorption of Gases, with Special Reference to the Evaluation of Surface Area and Pore Size Distribution (IUPAC Technical Report). Pure Appl. Chem. 2015, 87, 1051–1069. 10.1515/pac-2014-1117. [DOI] [Google Scholar]
  11. Peleg M. Models of Sigmoid Equilibrium Moisture Sorption Isotherms with and without the Monolayer Hypothesis. Food Eng. Rev. 2020, 12, 1–13. 10.1007/s12393-019-09207-x. [DOI] [Google Scholar]
  12. Odler I. The BET-Specific Surface Area of Hydrated Portland Cement and Related Materials. Cem. Concr. Res. 2003, 33, 2049–2056. 10.1016/S0008-8846(03)00225-4. [DOI] [Google Scholar]
  13. Zografi G.; Kontny M. J.; Yang A. Y. S.; Brenner G. S. Surface Area and Water Vapor Sorption of Macrocrystalline Cellulose. Int. J. Pharm. 1984, 18, 99–116. 10.1016/0378-5173(84)90111-X. [DOI] [Google Scholar]
  14. Gómez-Gualdrón D. A.; Moghadam P. Z.; Hupp J. T.; Farha O. K.; Snurr R. Q. Application of Consistency Criteria to Calculate BET Areas of Micro- and Mesoporous Metal-Organic Frameworks. J. Am. Chem. Soc. 2016, 138, 215–224. 10.1021/JACS.5B10266. [DOI] [PubMed] [Google Scholar]
  15. Sinha P.; Datar A.; Jeong C.; Deng X.; Chung Y. G.; Lin L.-C. Surface Area Determination of Porous Materials Using the Brunauer-Emmett-Teller (BET) Method: Limitations and Improvements. J. Phys. Chem. C 2019, 123, 20195–20209. 10.1021/acs.jpcc.9b02116. [DOI] [Google Scholar]
  16. Brunauer S.; Emmett P. H. The Use of Low Temperature van der Waals Adsorption Isotherms in Determining the Surface Areas of Various Adsorbents. J. Am. Chem. Soc. 1937, 59, 2682–2689. 10.1021/ja01291a060. [DOI] [Google Scholar]
  17. Guggenheim E. A.Applications of Statistical Mechanics; Clarendon Press: Oxford, 1966; pp 186–206. [Google Scholar]
  18. Anderson R. B. Modifications of the Brunauer, Emmett and Teller Equation. J. Am. Chem. Soc. 1946, 68, 686–691. 10.1021/ja01208a049. [DOI] [PubMed] [Google Scholar]
  19. de Boer J. H.Dynamical Character of Adsorption; Clarendon Press: Oxford, 1968; pp 200–219. [Google Scholar]
  20. Timmermann E. O. A BET-like Three Sorption Stage Isotherm. J. Chem. Soc., Faraday Trans. 1 1989, 85, 1631–1645. 10.1039/F19898501631. [DOI] [Google Scholar]
  21. Shimizu S.; Matubayasi N. Fluctuation Adsorption Theory: Quantifying Adsorbate-Adsorbate Interaction and Interfacial Phase Transition from an Isotherm. Phys. Chem. Chem. Phys. 2020, 22, 28304–28316. 10.1039/D0CP05122E. [DOI] [PubMed] [Google Scholar]
  22. Shimizu S.; Matubayasi N. Sorption: A Statistical Thermodynamic Fluctuation Theory. Langmuir 2021, 37, 7380–7391. 10.1021/acs.langmuir.1c00742. [DOI] [PMC free article] [PubMed] [Google Scholar]
  23. Shimizu S.; Matubayasi N. Adsorbate-Adsorbate Interactions on Microporous Materials. Microporous Mesoporous Mater. 2021, 323, 111254. 10.1016/j.micromeso.2021.111254. [DOI] [Google Scholar]
  24. Shimizu S.; Matubayasi N. Cooperative Sorption on Porous Materials. Langmuir 2021, 37, 10279–10290. 10.1021/acs.langmuir.1c01236. [DOI] [PMC free article] [PubMed] [Google Scholar]
  25. Shimizu S.; Matubayasi N. Temperature Dependence of Sorption. Langmuir 2021, 37, 11008–11017. 10.1021/ACS.LANGMUIR.1C01576. [DOI] [PubMed] [Google Scholar]
  26. Rouquerol J.; Avnir D.; Fairbridge C. W.; Everett D. H.; Haynes J. M.; Pernicone N.; Ramsay J. D. F.; Sing K. S. W.; Unger K. K. Recommendations for the Characterization of Porous Solids (Technical Report). Pure Appl. Chem. 1994, 66, 1739–1758. 10.1351/pac199466081739. [DOI] [Google Scholar]
  27. Kittel C.Elementary Statistical Physics; Dover Publications: New York, 2004; pp 117–125. [Google Scholar]
  28. Shimizu S. Estimating Hydration Changes upon Biomolecular Reactions from Osmotic Stress, High Pressure, and Preferential Hydration Experiments. Proc. Natl. Acad. Sci. U.S.A. 2004, 101, 1195–1199. 10.1073/pnas.0305836101. [DOI] [PMC free article] [PubMed] [Google Scholar]
  29. Shimizu S.; Boon C. L. The Kirkwood-Buff Theory and the Effect of Cosolvents on Biochemical Reactions. J. Chem. Phys. 2004, 121, 9147–9155. 10.1063/1.1806402. [DOI] [PubMed] [Google Scholar]
  30. Shimizu S.; Matubayasi N. Preferential Solvation: Dividing Surface vs Excess Numbers. J. Phys. Chem. B 2014, 118, 3922–3930. 10.1021/jp410567c. [DOI] [PubMed] [Google Scholar]
  31. Shimizu S.; Matubayasi N. Cooperativity in Micellar Solubilization. Phys. Chem. Chem. Phys. 2021, 23, 8705–8716. 10.1039/D0CP06479C. [DOI] [PubMed] [Google Scholar]
  32. Shimizu S.; Matubayasi N. Thermodynamic Stability Condition Can Judge Whether a Nanoparticle Dispersion Can Be Considered a Solution in a Single Phase. J. Colloid Interface Sci. 2020, 575, 472–479. 10.1016/j.jcis.2020.04.101. [DOI] [PubMed] [Google Scholar]
  33. Shimizu S.; Matubayasi N. Phase Stability Condition and Liquid–Liquid Phase Separation under Mesoscale Confinement. Phys. A 2021, 563, 125385. 10.1016/j.physa.2020.125385. [DOI] [Google Scholar]
  34. Langmuir I. The Adsorption of Gases on Plane Surfaces of Glass, Mica and Platinum. J. Am. Chem. Soc. 1918, 40, 1361–1403. 10.1021/ja02242a004. [DOI] [Google Scholar]
  35. Klobes P.; Meyer K.; Munro R. G.. Porosity and Specific Surface Area Measurements for Solid Materials; National Institute of Standards and Technology: Gaithersburg, MD, 2006; Vol. 960–17, p 79. [Google Scholar]
  36. Maruyama I.; Nishioka Y.; Igarashi G.; Matsui K. Microstructural and Bulk Property Changes in Hardened Cement Paste during the First Drying Process. Cem. Concr. Res. 2014, 58, 20–34. 10.1016/J.CEMCONRES.2014.01.007. [DOI] [Google Scholar]
  37. Aili A.; Maruyama I. Review of Several Experimental Methods for Characterization of Micro- and Nano-Scale Pores in Cement-Based Material. Int. J. Concr. Struct. Mater. 2020, 14, 1–18. 10.1186/S40069-020-00431-Y. [DOI] [Google Scholar]
  38. Pini R. Interpretation of Net and Excess Adsorption Isotherms in Microporous Adsorbents. Microporous Mesoporous Mater. 2014, 187, 40–52. 10.1016/j.micromeso.2013.12.005. [DOI] [Google Scholar]
  39. Siderius D.NIST/ARPA-E Database of Novel and Emerging Adsorbent Materials. 2020. 10.18434/T43882. [DOI]
  40. Kirkwood J. G.; Buff F. P. The Statistical Mechanical Theory of Solutions. J. Chem. Phys. 1951, 19, 774–777. 10.1063/1.1748352. [DOI] [Google Scholar]
  41. Schramm B.; Gehrmann R. Second Virial Coefficients of Nitrogen at Very Low Temperatures. J. Chem. Soc., Faraday Trans. 1 1979, 75, 479–480. 10.1039/F19797500479. [DOI] [Google Scholar]
  42. Schramm B.; Hebgen U. The Second Virial Coefficient of Argon at Low Temperatures. Chem. Phys. Lett. 1974, 29, 137–139. 10.1016/0009-2614(74)80151-X. [DOI] [Google Scholar]
  43. Harvey A. H.; Lemmon E. W. Correlation for the Second Virial Coefficient of Water. J. Phys. Chem. Ref. Data 2004, 33, 369–376. 10.1063/1.1587731. [DOI] [Google Scholar]
  44. Ben-Naim A.Molecular Theory of Solutions; Oxford University Press: Oxford, 2006; pp 112–135. [Google Scholar]
  45. Shimizu S. Formulating Rationally via Statistical Thermodynamics. Curr. Opin. Colloid Interface Sci. 2020, 48, 53–64. 10.1016/j.cocis.2020.03.008. [DOI] [Google Scholar]
  46. House W. A.; Jaycock M. J. The Application of the Gas–Solid Virial Expansion to Argon Absorbed on the (100) Face of Sodium Chloride. Proc. R. Soc. London, Ser. A 1976, 348, 317–337. 10.1098/rspa.1976.0041. [DOI] [Google Scholar]
  47. Okambawa R.; Benaddi H.; St-Arnaud J.-M.; Bose T. K. Gas-Solid Interaction and the Virial Description of the Adsorption of Methane on Steam-Activated Carbon. Langmuir 2000, 16, 1163–1166. 10.1021/la9901231. [DOI] [Google Scholar]
  48. de Torre L. E. C.; Flores E. S.; Llanos J. L.; Bottani E. J. Gas-Solid Potentials for N2, O2, and CO2 Adsorbed on Graphite, Amorphous Carbons, AI2O3, and TiO2. Langmuir 1995, 11, 4742–4747. 10.1021/la00012a027. [DOI] [Google Scholar]
  49. Ho R.; Heng J. Y. Y. A Review of Inverse Gas Chromatography and Its Development as a Tool to Characterize Anisotropic Surface Properties of Pharmaceutical Solids. KONA Powder Part. J. 2013, 30, 164–180. 10.14356/kona.2013016. [DOI] [Google Scholar]
  50. Jones M. D.; Young P.; Traini D. The Use of Inverse Gas Chromatography for the Study of Lactose and Pharmaceutical Materials Used in Dry Powder Inhalers. Adv. Drug Delivery Rev. 2012, 64, 285–293. 10.1016/j.addr.2011.12.015. [DOI] [PubMed] [Google Scholar]
  51. Gullingsrud J. R.; Braun R.; Schulten K. Reconstructing Potentials of Mean Force through Time Series Analysis of Steered Molecular Dynamics Simulations. J. Comput. Phys. 1999, 151, 190–211. 10.1006/jcph.1999.6218. [DOI] [Google Scholar]
  52. De Pablo P. J. Introduction to Atomic Force Microscopy. Methods Mol. Biol. 2011, 783, 197–212. 10.1007/978-1-61779-282-3_11. [DOI] [PubMed] [Google Scholar]
  53. Keii T.; Takagi T.; Kanetaka S. A New Plotting of the BET Method. Anal. Chem. 1961, 33, 1965. 10.1021/ac50154a063. [DOI] [Google Scholar]

Associated Data

This section collects any data citations, data availability statements, or supplementary materials included in this article.

Supplementary Materials

la2c00753_si_001.pdf (272.7KB, pdf)

Articles from Langmuir are provided here courtesy of American Chemical Society

RESOURCES