Seishi Shimizu1, Nobuyuki Matubayasi2. 1. York Structural Biology Laboratory, Department of Chemistry, University of York, Heslington, York YO10 5DD, U.K. 2. Division of Chemical Engineering, Graduate School of Engineering Science, Osaka University, Toyonaka, Osaka 560-8531, Japan.
Abstract
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.
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.
Specific
surface area is one of the major characteristics of materials
as adsorbents.[1−5] 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,[1−3,11,12] 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 food[11] 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 a).[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.[3,11−13]
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 ) can be derived
by incorporating the sorbate-interface (blue), sorbate–sorbate
(green), and sorbate triplet (orange) interactions in the Maclaurin
expansion (eq ). 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).
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 ) can be derived
by incorporating the sorbate-interface (blue), sorbate–sorbate
(green), and sorbate triplet (orange) interactions in the Maclaurin
expansion (eq ). 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 ) that[3,10,14,15]
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 , 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.
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 , 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 b);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/p0”[10] (where n is the amount of sorption, Figure c);C. the value of the monolayer capacity “should
correspond
to a relative pressure p/p0 falling within the selected linear region” (Figure b);[14] andD. “[t]he relative pressure corresponding to the
monolayer
loading calculated from BET theory [] should be
equal to the pressure determined
in criterion [C],”[14] with the tolerance
of 20% (Figure a).[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:[1−3,6,11,12,16] “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,[17−19] 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 ).[21−25] 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 b,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: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.to start from the
universal statistical
thermodynamic principles of sorption (Figure b),to translate what the BET monolayer
capacity and the BET surface area mean in the language of statistical
thermodynamics and molecular interaction (Figure c), andto 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.
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 a). We derive the
statistical thermodynamic isotherm via the Maclaurin expansion, incorporating
sorbate-interface, sorbate–sorbate, and sorbate triplet interactions
(Figure b,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
theory[22] 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 ⟨n2s⟩,
is expressed as[21]where F is the free energy
of the interface (Figure b). Equation 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⟩
– ⟨n2s⟩, depends on the sorbate activity a2 can be characterized through its derivativein terms of the difference
in sorbate–sorbate number correlations between the interface,
⟨δn2δn2⟩, and the vapor and solid reference systems,
⟨δn2gδn2g⟩ and ⟨δn2sδn2s⟩, with δn2 ≡ n2 – ⟨n2⟩, δn2g ≡ n2g – ⟨n2g⟩, and δn2s ≡ n2s – ⟨n2s⟩ defined as the deviations from the
mean sorbate numbers, respectively. (The background material for the
derivation of eq from eq can be found, e.g., in
p 129, eq 25.19 of ref (27)). How the isotherm depends on a2, according
to eq , 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 as the generalization
of our previous paper,[22] asHere, the
sorbate excess number
around a probe sorbate, N22, together
with the corresponding quantities for the reference states (N22g and N22s) have been introduced and defined as[21,22](In deriving eq , the number–number correlations appearing from
differentiating the numbers using eq are replaced via eq by the excess numbers.) The excess number is used
universally in solutions,[28−30] interfaces,[21−23] surfactants,[31] nanoparticles,[32] and
confined systems.[33] The utility of eq can best be seen in its
following integrated formwhere A0 is a constant of integration (whose physical
interpretation
will be clarified below). Introducing the Maclaurin expansion of eq and combining it
with eq yields the
following general
isotherm (Figure c)Equation is our statistical thermodynamic isotherm.
Our previous theory[21,22] results from ⟨n2⟩ – ⟨n2g⟩
– ⟨n2s⟩ ≃ ⟨n2⟩ as shown in the Supporting Information. We will later demonstrate that eq 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 c). This can be achieved by the relationship between a2 and the gas-phase density, c2g, via a2 = c2g/c2, 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, as[22]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 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 c). 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 c). 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 before[22] 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 ) 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 GAB[17−19] 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 a) into statistical thermodynamics (Figure b,c, step II in Introduction). The BET model has the following functional
form:Comparing eqs and 10a leads
to the following correspondence between the BET parameters and statistical
thermodynamicsOr equivalentlyThus, the BET model parameters have been given
a statistical thermodynamic interpretation by eq , in combination with eqs 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 ) with the statistical thermodynamic isotherm (eq ) 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 is modified asand the integration of eq is changed towith the
constants Ar, Br, and Cr defined at a2 = ar. Ar is now linked to the surface–sorbate Kirkwood–Buff
integral at a2 = arand Br is related to the sorbate number fluctuations at a2 = ar asAlso, 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 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 and 10b leads to the
following relationshipEquation can be considered as a special case (ar → 0) of the “interfacial capacity”
defined aswhich
is valid both for
the regional isotherm around a2 = ar as well as the global isotherm (ar → 0). Equation is the statistical thermodynamic generalization of
the monolayer capacity. Using eq , eq can
be rewritten asEquation allows nI to be calculated from any fitting equation.
A practical approach
is to apply eq instead
of eq to carry out
regional isotherm fitting within a range of finite a2. Combining eq with eq ,
we obtain the following simple expressionIn addition to our isotherm (eq ), other isotherm models
can also
be used with eq .
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
The statistical
thermodynamic isotherm will
replace the BET model as its model-free generalization.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.Complications due to the BET model
assumptions (Figure a) will be eliminated,
leading to an easier fitting of isotherm data using the statistical
thermodynamic isotherm (Figure c) 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.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 ), which can be rewritten
asWe 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 and 10c. In the BET model, the
three parameters are not independent; eq reveals the following constraint for the
BET modelthrough which eq can be rewritten aswhich is identical to the well-known BET plot
shown indeed in Figure b.[9,10] To summarize, the BET plot (eq ) contains only two independent
parameters compared to three (eq ) due to the BET model assumption (eq ).
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 ), which does not
involve the constraints imposed by the BET (eq ) or Langmuir (C0 = 0) models. To demonstrate this systematically, we have chosen
the following systems as examples.Carrying out the BET analysis via eq (Figures b, 4b, and 5b) and determining the parameters for the statistical
thermodynamic
isotherm via eq (Figures c, 4c, and 5c) reveal their varying degrees
of closeness to the BET and Langmuir models.
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 ), 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) plot (eq ) with
the fitting parameters listed in Table .
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 ). Dotted lines: linear
fit based on data between a2 = 0.2 and
0.3 with the unphysical intercepts of (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 (red) and −0.0034 (black). (c) plot (eq ) with
the fitting parameters listed in Table . The dashed and dotted lines
were calculated under the BET (C0 = 2(A0 – B0))
and Langmuir (C0 = 0) constraints.
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 ). Solid
lines: linear fit based on data between a2 = 0.05 and 0.3 with the unphysical intercepts of (red) and −3.05 (black), respectively.
(c) plot (eq ) with the fitting parameters listed in Table . The dashed and dotted lines
were calculated under the BET (C0 = 2(A0 – B0))
and Langmuir (C0 = 0) constraints.
The adsorption isotherms of water and
nitrogen on a Portland cement paste (Figure a) measured by Maruyama et al.[36,37]The adsorption of
argon and nitrogen
on zeolite 13X (Figures a and 5a) measured by Pini[38,39] and chosen by Rouquerol et al.[3] to illustrate
the difficulties of applying the BET analysis to microporous systems.[9,10]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 ), 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) plot (eq ) with
the fitting parameters listed in Table .
Table 1
Parameters for the Statistical Thermodynamic
Isotherm and a Test of Closeness to the BET (C0 = 2(A0 – B0)) 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
All R2 values were above 0.9987.
Data reported by Maruyama et al.[36,37]
Data reported by Pini.[38]
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 ). Dotted lines: linear
fit based on data between a2 = 0.2 and
0.3 with the unphysical intercepts of (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 (red) and −0.0034 (black). (c) plot (eq ) with
the fitting parameters listed in Table . The dashed and dotted lines
were calculated under the BET (C0 = 2(A0 – B0))
and Langmuir (C0 = 0) constraints.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 ). Solid
lines: linear fit based on data between a2 = 0.05 and 0.3 with the unphysical intercepts of (red) and −3.05 (black), respectively.
(c) plot (eq ) with the fitting parameters listed in Table . The dashed and dotted lines
were calculated under the BET (C0 = 2(A0 – B0))
and Langmuir (C0 = 0) constraints.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?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 b) and by the value of C0 being not too far from the BET constraint, that is, 2(A0 – B0) (eq ) as shown in Table .The BET analysis
for zeolite (Figures b and 5b) leads to difficulties (as will be
discussed below) because
the isotherms do not satisfy the condition for the BET model, C0 = 2(A0 – B0). Judging from the value of C0 (Table ), 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 ).All R2 values were above 0.9987.Data reported by Maruyama et al.[36,37]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 ). (Such a process is unnecessary for an isotherm which
strictly obeys the BET model, Figure b.) 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 b). For zeolites,
the a2 regions within this guideline,
0.05 ≤ a2 ≤ 0.1 and 0.20
≤ a2 ≤ 0.3 for Figure b and 0.05 ≤ a2 ≤ 0.3 for Figure b, gave negative values for the intercept
( in eq ) 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 ). 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
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
See the list in the Introduction.
R2 values
were above 0.9996.
Units
in mmol/g.
Units in m2/g.
See the list in the Introduction.R2 values
were above 0.9996.Units
in mmol/g.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 ) that is
not satisfied (Table ). Therefore, eq , free of the BET assumptions, can fit the experimental isotherm
over a range of a2 between a2 = 0 and 0.4 (Figures c and 5c), much wider than the
linear regions of the BET plot (Table ). A straightforward analysis is afforded by the general
statistical thermodynamic formula without any constraints on its parameters
(eq ).
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 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 as[21,22]which is a
simplified version of eq 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, as[21,28,30,40]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 coefficients[41−43] (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 ) is the ar →
0 limit of the interfacial capacity (eq ), which can be simplified asFor the monolayer capacity to be
positive,
as postulated by the BET model,[3,9,10]G22 at ar → 0 must be negative. This is underscored by the statistical
thermodynamic expression of the BET constant simplified in combination
of eqs , 9, 10c, and 11b aswhere c2 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 and 10c). This seemingly surprising conclusion can be supported also
from a perspective based purely on the BET plot (eq , Figures b and 5b). The monolayer
capacity nm and the BET constant CB are evaluated from its gradient () and intercept (), 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 experimentally[46−52] is summarized in the Supporting Information). Extrapolation requires a fitting function. However, even with
the use of the general polynomial free of BET (eq ), 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 plot for argon (Figure ) corresponds (via eq ) 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
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 ) which exhibits a negative gradient at a2 → 0. (c) plot with the fitting equation (eq with C0 = 0) using data
between a2 = 4 × 10–4 and 1 × 10–3.
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 ) which exhibits a negative gradient at a2 → 0. (c) plot with the fitting equation (eq 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(A0 – B0) (Table ). 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 ) and zeolite 13X (Figure ).) Combining eqs and 15a under ⟨n2⟩ – ⟨n2g⟩
– ⟨n2s⟩ ≃ ⟨n2⟩ (Supporting Information), we obtainAt Point M, (a2 = aM), must be
satisfied, which leads to
Figure 7
(a) Adsorption of water (blue circles) and nitrogen
(black squares)
on a Portland cement paste (Figure ), with the indication of the respective amounts of
adsorption at Point M, ⟨n2⟩M at a2 = aM, calculated using eqs and 18d. nm is the corresponding BET monolayer capacity determined in Table . (b) Excess numbers
of sorbates around a probe sorbate, N22, calculated using eq (with the parameters from Table ) for water (blue circles) and nitrogen (black squares).
Point M, where N22 is minimum, is calculated
using eq .
Figure 8
(a) Adsorption of argon on crystalline (red squares) and pelleted
(black circles) on zeolite 13X (Figure ), with the indication of the respective amounts of
adsorption at Point M, ⟨n2⟩M at a2 = aM, calculated using eqs and 18d. nm is the corresponding BET monolayer capacity determined in Table . (b) Excess numbers
of sorbates around a probe sorbate, N22, calculated using eq (with the parameters from Table ) for crystalline (red squares) and pelleted (black
circles) zeolite 13X. Point M, where N22 is minimum, is calculated using eq .
(a) Adsorption of water (blue circles) and nitrogen
(black squares)
on a Portland cement paste (Figure ), with the indication of the respective amounts of
adsorption at Point M, ⟨n2⟩M at a2 = aM, calculated using eqs and 18d. nm is the corresponding BET monolayer capacity determined in Table . (b) Excess numbers
of sorbates around a probe sorbate, N22, calculated using eq (with the parameters from Table ) for water (blue circles) and nitrogen (black squares).
Point M, where N22 is minimum, is calculated
using eq .(a) Adsorption of argon on crystalline (red squares) and pelleted
(black circles) on zeolite 13X (Figure ), with the indication of the respective amounts of
adsorption at Point M, ⟨n2⟩M at a2 = aM, calculated using eqs and 18d. nm is the corresponding BET monolayer capacity determined in Table . (b) Excess numbers
of sorbates around a probe sorbate, N22, calculated using eq (with the parameters from Table ) for crystalline (red squares) and pelleted (black
circles) zeolite 13X. Point M, where N22 is minimum, is calculated using eq .Solving eq under B0 <
0 for sorbate–sorbate
exclusion,[22] we obtainConsequently, the amount of adsorption at
Point M can be calculated using eqs and 18b asRestricting our result (eq ) to the BET model using eq , we obtain the following
expression for the amount of adsorption at Point MThe approximation at the
final step is accurate for large CB. The
location of aM can also be specified asEquations 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, 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 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 ) and even for
the statistical thermodynamic isotherm (eq ). Therefore, the amount of adsorption at
Point M ⟨n2⟩M is a viable alternative for the estimation of the monolayer capacity, nm. Indeed, ⟨n2⟩M, calculated via eq , agrees reasonably with the monolayer capacity
calculated from the BET analysis (Table , which reports a comparison between the
statistical thermodynamic surface area ⟨n2⟩Mσm with the BET surface
area nmσm, using the
standard values of sorbate cross-sectional areas). Point M values
can be calculated precisely by eq , and their location around the knee can be inspected
visually by Figures 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 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
sorbate–sorbent
fitting a2 range
aM
⟨n2⟩M mmol/g
(N22)M
stat therm
surface area (STSA) m2/g
BET
surface
area m2/g (Table 2)
eq 18c
eq 18d
eq 18a
⟨n2⟩Mσmd
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
Data reported by
Maruyama et al.[36,37]
Data reported by Pini.[38]
A narrower fitting range was
not
feasible due to the sparseness of data around aM
We have used the
cross-sectional
area, σ, 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]
Compared to 196 and 113 m2/g by Aili
and Maruyama.[37]
Data reported by
Maruyama et al.[36,37]Data reported by Pini.[38]A narrower fitting range was
not
feasible due to the sparseness of data around aMWe have used the
cross-sectional
area, σ, 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]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 ) around the knee (Figures 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 ) 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. ⟨n2⟩M is also defined clearly
as the net excess sorbate–surface distribution function[21,22] 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 , 18a, 18e, and 18f asUsing eq , a one-to-one correspondence between CB and (N22)M can
be established for the BET model (Figure ). 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 ⟨n2⟩M/(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
Relationship
between the BET constant, CB, and the
excess number of sorbates around a probe sorbate, (N22)M, at Point M plotted using eq 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.
Relationship
between the BET constant, CB, and the
excess number of sorbates around a probe sorbate, (N22)M, at Point M plotted using eq 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 ) but is different from the Portland cement isotherms
(Figure , Table ). N22 ≃ −1 at Point M is equivalent toA physical picture of Point M adsorption
emerges from (a)–(c)
for this case (Figure ). 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]a very
small sorbate number variance,
⟨δn2δn2⟩ ≃ 0, at Point M, according to eq ;approximately one sorbate molecule in
total being excluded around a probe sorbate, N22 ≃ −1 at Point M, according to eq ; andthe amount of adsorption is close to
the interfacial capacity at Point M, (nI)M ≃ ⟨n2⟩M, according to eq .
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 ). The existence of a sharp knee corresponds to N22 below −0.78 (Figure ). 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 ). Compared to N22 ≃ −1 at Point M, this case shows thatThus, 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.the sorbate
number variance, ⟨δn2δn2⟩,
is larger (eq );when a probe sorbate is
placed, less
than one sorbate is excluded (eq ); andthe amount
of adsorption is smaller
than the interfacial capacity at Point M, (nI)M > ⟨n2⟩M (eq ).
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 ). 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 ). 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 ), water fails the IUPAC recommendation of CB > 80 while nitrogen satisfies it. Microscopically,
⟨n2⟩M = 0.55(nI)M (eq ) 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:Note that a2 and ⟨n2⟩ correspond directly to p/p0 and n of the IUPAC
notation, respectively. Hence, aM and
⟨n2⟩M are simply p/p0 and n at
Point M, respectively. Here are the considerations for a sense check:Fit an experimental isotherm around
its knee using eq (Figures c, 4c, and 5c, and Table ).Calculate the location of Point M (aM) using eq and the amount of adsorption at Point M (⟨n2⟩M) eq (Table ).Estimate the surface
area by multiplying
⟨n2⟩M by the
probe molecule’s cross-sectional area σm (Table ). This can be called
the statistical thermodynamic surface area (STSA) as an alternative
for the BET surface area.the location of aM and ⟨n2⟩M are roughly around the
knee of an isotherm (Figure a and 8a);the calculated aM via eq is indeed at the minimum
of N22 (Figures b and 8b);N22 at Point
M is between
−0.78 and −0.84 for a sign of monolayer coverage (Figures b, 8b, and 9). The value of N22 should be quoted with STSA.This range of N22 is the
statistical thermodynamic translation of the IUPAC guideline[10] 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: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.The interface can
be approximated
as a planar monolayer.The standard value of the probe’s
cross-sectional area is valid.
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 filling[14] 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 b 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 fromThe 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, hastrying to fit the BET model to the isotherms
that break its basic assumptions; andambiguous and unclear physical meanings
of the BET constant and the monolayer capacityshown 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; andtranslated 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 areThis 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 rolethe excess
number N22, a measure of sorbate–sorbate
interaction at
the interface, as central to interfacial coverage;Point M, at which N22 takes the minimum value, as the precise location of
interfacial coverage; andadsorption at Point M replaces the
monolayer capacity for calculating the surface area.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; andas 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.
Authors: Diego A Gómez-Gualdrón; Peyman Z Moghadam; Joseph T Hupp; Omar K Farha; Randall Q Snurr Journal: J Am Chem Soc Date: 2015-12-24 Impact factor: 15.419