Matthew Witman1, Sanliang Ling2, Sudi Jawahery1, Peter G Boyd3, Maciej Haranczyk4,5, Ben Slater2, Berend Smit1,3. 1. Department of Chemical and Biomolecular Engineering, University of California , Berkeley, California 94720, United States. 2. Department of Chemistry, University College London , 20 Gordon Street, London WC1H 0AJ, United Kingdom. 3. Laboratory of Molecular Simulation, Institut des Sciences et Ingénierie Chimiques, Valais, Ecole Polytechnique Fédérale de Lausanne (EPFL) , Rue de l'Industrie 17, CH-1951 Sion, Switzerland. 4. Computational Research Division, Lawrence Berkeley National Laboratory , Berkeley, California 94720, United States. 5. IMDEA Materials Institute , C/Eric Kandel 2, 28906 Getafe, Madrid, Spain.
Abstract
For applications of metal-organic frameworks (MOFs) such as gas storage and separation, flexibility is often seen as a parameter that can tune material performance. In this work we aim to determine the optimal flexibility for the shape selective separation of similarly sized molecules (e.g., Xe/Kr mixtures). To obtain systematic insight into how the flexibility impacts this type of separation, we develop a simple analytical model that predicts a material's Henry regime adsorption and selectivity as a function of flexibility. We elucidate the complex dependence of selectivity on a framework's intrinsic flexibility whereby performance is either improved or reduced with increasing flexibility, depending on the material's pore size characteristics. However, the selectivity of a material with the pore size and chemistry that already maximizes selectivity in the rigid approximation is continuously diminished with increasing flexibility, demonstrating that the globally optimal separation exists within an entirely rigid pore. Molecular simulations show that our simple model predicts performance trends that are observed when screening the adsorption behavior of flexible MOFs. These flexible simulations provide better agreement with experimental adsorption data in a high-performance material that is not captured when modeling this framework as rigid, an approximation typically made in high-throughput screening studies. We conclude that, for shape selective adsorption applications, the globally optimal material will have the optimal pore size/chemistry and minimal intrinsic flexibility even though other nonoptimal materials' selectivity can actually be improved by flexibility. Equally important, we find that flexible simulations can be critical for correctly modeling adsorption in these types of systems.
For applications of metal-organic frameworks (MOFs) such as gas storage and separation, flexibility is often seen as a parameter that can tune material performance. In this work we aim to determine the optimal flexibility for the shape selective separation of similarly sized molecules (e.g., Xe/Kr mixtures). To obtain systematic insight into how the flexibility impacts this type of separation, we develop a simple analytical model that predicts a material's Henry regime adsorption and selectivity as a function of flexibility. We elucidate the complex dependence of selectivity on a framework's intrinsic flexibility whereby performance is either improved or reduced with increasing flexibility, depending on the material's pore size characteristics. However, the selectivity of a material with the pore size and chemistry that already maximizes selectivity in the rigid approximation is continuously diminished with increasing flexibility, demonstrating that the globally optimal separation exists within an entirely rigid pore. Molecular simulations show that our simple model predicts performance trends that are observed when screening the adsorption behavior of flexible MOFs. These flexible simulations provide better agreement with experimental adsorption data in a high-performance material that is not captured when modeling this framework as rigid, an approximation typically made in high-throughput screening studies. We conclude that, for shape selective adsorption applications, the globally optimal material will have the optimal pore size/chemistry and minimal intrinsic flexibility even though other nonoptimal materials' selectivity can actually be improved by flexibility. Equally important, we find that flexible simulations can be critical for correctly modeling adsorption in these types of systems.
Metal–organic
frameworks (MOFs) have garnered significant
attention in the scientific community due to their potential applications
ranging from gas storage and separations to catalysis and sensors.[1−6] The diversity of applications for which MOFs are currently being
investigated arises primarily from their highly tunable chemical and
geometric properties since the combinatorics of their nodal composition,
consisting of secondary building units (SBUs) and ligands, leads to
an enormous number of possible structures.[7] An interesting consequence of such structural diversity is that
the flexibility of these materials can be exploited in various ways
to yield improved performance in a variety of applications.[8] Focusing on gas storage and separations, flexibility
has been experimentally and computationally examined in the contexts
of breathing,[9−11] swelling,[12] rotatable
and flexible linkers,[13,14] shape memory,[15] complex lattice deformation,[16] subnetwork displacement,[17] negative gas
adsorption,[18,19] and its strong influence on diffusion,[20] all with the ultimate goal of exploiting these
phenomena to obtain desirable adsorption properties. Such breadth
presents interesting challenges and opportunities for experimental
and computational characterization of flexibility in MOFs and for
determination of how it can be utilized for the design of better gas
adsorbents.MOFs with dynamic constituents (i.e., rotatable
and flexible ligands)[13] have pore spaces
that can change in size and/or
shape, while the unit cell volume and shape remains constant. A natural
question that arises is whether this phenomenon can be optimized for
specific applications in gas separations, and our work highlights
how controlling this intrinsic flexibility of MOFs can optimize these
materials for shape selective adsorption. An example of such an application
is the separation of Xe/Kr mixtures where the most selective materials
have a pore size and shape commensurate with the adsorbates,[21] and thus we illustrate our findings in the context
of the widely studied Xe/Kr separations.[22,23]To study the effect of intrinsic flexibility on the separation
of tight fitting molecules, we have developed a simple model that
allows us to compute the selectivity in the Henry regime as a function
of the flexibility of a material. Our model quantitatively and systematically
demonstrates that intrinsic flexibility can either increase or decrease
selectivity for a given material based on its pore size characteristics.
However, an interesting consequence will follow: Achieving the globally optimal separation performance necessitates not
only having a material with the ideal pore size and chemistry but
also finding materials that simultaneously minimize intrinsic flexibility.
Next we compare these results to Xe/Kr adsorption data obtained from
screening the CoRE MOF database[24] when
each structure’s flexibility is modeled via a classical force
field (FF) recently used in the literature.[25] It is important to note that when high-throughput computational
studies are employed to elucidate stucture–property relationships,[26−29] they are almost exclusively performed using the rigid structure
approximation (see details of ref (30) for the only exception to our knowledge). This
approximation is considered a safe assumption when thermodynamic fluctuations
are assumed to average out the framework atoms’ locations to
their initial values, and so intrinsic flexibility is assumed to have
no effect. However, by relaxing this approximation and using flexible
simulations to screen a database of MOFs, we observe that flexibility
has the same impact on adsorption behavior trends as shown by the
analytical model. We then select several MOFs from the screening to
study in further detail the effect of flexibility on each material’s
performance in Xe/Kr separations and finally show that flexibility
is necessary to yield better agreement with experimental adsorption
data of a high performance MOF system known as SBMOF-1.[23] Thus, we not only quantitatively and systematically
demonstrate the impacts of flexibility on shape selective adsorption
through models and simulations but also are able to answer the more
fundamental question of whether controlling intrinsic flexibility
can optimize material performance in this type of separation application.
Methods: Analytical Model
The
effects of intrinsic flexibility in MOFs on Henry regime adsorption
are elucidated by an analytical model of a flexible pore and direct
simulations of flexible MOF materials. The details of the direct simulations
are explained in the Methods: Direct Simulations section. For our analytical model, we construct a spherical pore
of radius Rp consisting of a wall of carbon
atoms. The visualization of this model is presented in Figure . A continuum approximation[31] is invoked such that an adsorbate does not interact
with discrete atomic centers but rather with a uniform surface density
of atoms, η = 1 atom /(π × 1.2 Å2). This surface density is chosen to be slightly higher than that
of graphene since adsorbates can interact with atoms beyond the pore
wall in real MOF materials. This approximation will permit an integrable
expression for the Henry coefficient, or the measure of a material’s
affinity for an adsorbate in the limit of infinite dilution.[32]
Figure 1
Visualization of a cross-section of the spherical pore
model. The
blue circle represents the adsorbate, and the gray spheres represent
the pore wall carbon atoms whose interaction energies are “smeared”
across the surface of the sphere with uniform density η. Due
to the spherical symmetry, the total adsorption energy of an adsorbate
at a given location r′ is simply an integral
over the azimuth angle ϕ.
Visualization of a cross-section of the spherical pore
model. The
blue circle represents the adsorbate, and the gray spheres represent
the pore wall carbon atoms whose interaction energies are “smeared”
across the surface of the sphere with uniform density η. Due
to the spherical symmetry, the total adsorption energy of an adsorbate
at a given location r′ is simply an integral
over the azimuth angle ϕ.The adsorption energy of one adsorbate within the spherical
pore
is dependent only on the r coordinate due to spherical
symmetry, as shown in Figure . Determination of this energy requires an integration of
the host–adsorbate interaction across the pore surface, which
in turn requires an expression for the distance between the adsorbate
and any point on the surface, given by d in eq :When the interactions between
the adsorbate and the pore wall are
computed by a pairwise Lennard-Jones potential and smeared across
the entire surface of the sphere rather than computed by discrete
pairwise distances (as is the case in a direct simulation), the total
adsorption energy takes the form of the integral in eq :where ϵ is the depth of the potential
energy well and σ is the distance
between the adsorbate and the wall
at which the potential energy is zero. Using this expression for the
adsorbate interaction energy, we can now calculate the Henry coefficient,
which is often computed in simulations via the expectation value in eq :[32]where β is (kBT)−1 and U+ is the total interaction energy of a randomly inserted ghost
adsorbate. This expectation value can be rewritten as an integral
over the pore volume by substitution of eq for U+. The resulting eq yields an integrable formula
for the rigid pore Henry coefficient (KH,r) for a given radius Rp with spherical
volume Vp:Next, flexibility is introduced into the model
by allowing Rp to change according to
a Gaussian distribution.
Now the flexible Henry coefficient (KH,f) is a function of the mean pore radius, ⟨Rp⟩, and the width of the Gaussian distribution
of the radius, σp, as shown in eq :The pore radius is bounded between Rmin and Rmax. Note
that in the limiting case as σp approaches 0, the
Gaussian distribution becomes a delta function, δ(⟨Rp⟩), and we recover the rigid pore approximation
such that KH,f(⟨Rp⟩, 0) = KH,r(⟨Rp⟩). Hence the KH,f can be calculated over a range of average pore radii and
distribution widths to demonstrate how the Henry coefficient depends
on both the average size and strength of fluctuations inside a flexible
pore. KH,f is calculated for both Xe and
Kr (KH,fXe and KH,fKr, respectively) and the infinite dilution
selectivity of the flexible model, Sf follows
as the ratio of these two quantities in eq . The selectivity of the rigid model is just
the ratio of the rigid Henry coefficients in eq :
Methods: Direct Simulations
In
addition to the analytical model, direct simulations are employed
using various computational techniques to demonstrate the effects
of intrinsic flexibility on the Henry regime adsorption properties
in MOFs. Ideally one would like to exclusively use ab initio calculations to describe such flexibility, but these are prohibitively
expensive for large systems and long simulation times that are required
to obtain sufficiently accurate results for these materials. Therefore,
we rely on force-field-based molecular simulations and corroborate
their performance with ab initio methods on a computationally
feasible system. We elaborate the details of these simulation techniques
starting with the description of the force fields used for classical
molecular dynamics (MD) simulations of flexible materials, followed
by a description of ab initio MD based on density
functional theory (DFT). Finally we describe how the Henry coefficients
are evaluated in these flexible materials as well as the calculation
of geometric properties which are necessary to evaluate how the pore
sizes change in MOFs between the rigid approximation and flexible
simulations.
Force Field Computed Framework Dynamics
There exists
a large diversity of metal–ligand chemistry in the CoRE MOF
database[24] (here we only study the materials
for which density derived electrostatic and chemical, or DDEC, charges[33] have been obtained), the entirety of which cannot
be described by any single classical force field (Dreiding,[34] UFF,[35] BTW,[36] UFF4MOF,[37] etc.).
In order to treat all materials on equal footing, we utilize the universal
force field (UFF) for all framework bonded potentials except for the
coordination bonds between metals and organic species. For bond and
angle potentials that are centered on the metal ions, the equilibrium
harmonic bond length and equilibrium harmoic angle are modified to
the crystallographic values read from the structure file.[25] This approximation is quite useful in that it
allows us to simulate framework dynamics in the canonical ensemble,
i.e., constant number of particles, volume, and temperature (NVT),
for a vast majority of the CoRE MOF structures without significant
unphysical distortions in the framework resulting from poor fits to
UFF geometries. In a previous work we have demonstrated that this
approximation is even sufficient to capture bulk moduli trends as
calculated by DFT in various MOFs.[25] This
force field is hereon referred to as UFF-fix-metal (UFF-FM), and details
on its implementation are presented in the SI.To benchmark our classically generated dynamics using the
UFF-FM approximation, we additionally performed an in-depth investigation
of framework dynamics for one particular MOF, known as SBMOF-1[38] with reference code KAXQIL in the Cambridge
Structural Database (CSD) that displays excellent Xe selectivity.[23] We implement an additional classical force field
which models metal–ligand coordination solely through Lennard-Jones
interactions and electrostatics whereby dummy cation beads serve to
delocalize the charge of the metal ion and preserve the octahedral
geometry of the Ca2+ ions in the framework. While the model
was originally developed to simulate solvation of cations,[39] recent work has illustrated this model’s
applicability in simulating MOF dynamics and deformation.[16] All potentials other than the metal–ligand
interactions were modeled with standard UFF potentials, and the model
is hereon referred to as the UFF-cationic-dummy-model (UFF-CDM) with
additional implementation details provided in the SI.For generating an ensemble of structures from a
MD run over which
the Henry coefficient can be computed, each CoRE MOF from ref (24) was simulated with UFF-FM
in the NVT ensemble using the open source LAMMPS software package
(http://lammps.sandia.gov).[40] The Nose–Hoover thermostat
was used with a temperature of 298 K, and the structure was equilibrated
for 30 ps, followed by a production run of 30 ps. During the production
run, a framework configuration was saved every ps to give a total
of 30 snapshots upon which the Henry coefficients could be calculated
via the ensemble average in eq . Justification for the number of snapshots necessary is elaborated
in the Porosity Characterization section.
The same MD methods were used to simulate SBMOF-1 with UFF-CDM. Charges
for UFF-FM simulations were taken from ref (24), while charges for UFF-CDM were derived from
electronic structure calculations (see the subsequent section) and
calculated according to the procedure discussed in the SI. Each MOF was simulated with periodic boundary
conditions, and a cutoff radius of 12.5 Å was imposed for nonbonded
interactions. Supercells were generated such that the perpendicular
components of the cell vectors were at least two times the cutoff
radius.
Ab Initio Computed Framework Dynamics
All DFT calculations have been performed using the CP2K code, which
uses a mixed Gaussian/plane-wave basis set.[41,42] We employed double-ζ polarization quality Gaussian basis sets[43] and a 400 Ry plane-wave cutoff for the auxiliary
grid, in conjunction with the Goedecker–Teter–Hutter
pseudopotentials.[44,45] All DFT calculations, including
single point energies, geometry/cell optimizations, and ab
initio molecular dynamics simulations (AIMD), were performed
using the PBE functional,[46] with Grimme’s
D3 van der Waals correction (PBE+D3).[47] This method was shown to give very good agreement with experimental
structural data on several MOFs which we studied previously[48,49] and on rare gas dimers and trimers.[47,50] The counterpoise
method[51] was used to correct for basis
set superposition errors in all binding energy calculations. AIMD
simulations within the Born–Oppenheimer approximation were
performed in the canonical (NVT) ensemble at the PBE+D3 level of theory.
A time step of 0.5 fs was used for the integration of the equation
of motion. Different supercell sizes were considered for the AIMD
simulations, and each AIMD simulation was performed for a duration
of 10 ps (20,000 MD steps following 2000 MD steps of equilibration
run with a strong thermostat coupling) and at a temperature of 298
K, which was controlled by the canonical sampling through velocity
rescaling thermostat[52] using a time constant
of 50 fs. The initial structure was taken from the experimentally
resolved crystal structure of SBMOF-1 and geometry optimized.[38]For implementation of UFF-CDM, partial
atomic charges are also needed (see SI).
The partial atomic charge analysis was performed using the REPEAT
method proposed by Campana et al.,[53] which
was recently implemented into the CP2K code based on a restrained
electrostatic potential framework.[54] We
have used charges determined from this scheme recently in our grand
canonical Monte Carlo simulations of CO2 adsorption in
MOF-74,[29,55] and we obtained very good agreement with
experiment on adsorption isotherms.
Flexible Henry Coefficient
Calculation
The Henry coefficient, KH, was previously defined in eq as the Boltzmann weighted average
of the interaction energy of a randomly inserted ghost particle,[32] and it measures a material’s affinity
for an adsorbate in the limit of infinite dilution. This quantity
can be simulated in porous materials by the Widom insertion method,[56] and in the rigid pore approximation, the average
in eq is calculated
by attempting ghost particle insertions on the single framework configuration
specified by experimental single crystal X-ray diffraction or by DFT
optimization. For flexible materials, however, we compute this ensemble
average over many different framework snapshots generated from a MD
simulation rather than just a single configuration. For both the rigid
and the flexible framework simulations, the same force field is used
to describe the nonbonded framework–adsorbate interactions.
These nonbonded interactions are modeled with a pairwise Lennard-Jones
potential where the framework atom ϵ and σ parameters
are taken from the UFF,[35] and the noble
gas ϵ and σ parameters are taken from the force field
of Boato.[57] Individual pairwise interaction
parameters are obtained by Lorentz–Berthelot mixing rules.
The Widom insertions for both the flexible and rigid Henry coefficients
described above were performed in the RASPA software package[58] at a temperature of 298 K.
Porosity Characterization
A geometric description of
porous materials known as the pore size distribution (PSD) was calculated
in the Zeo++ software package[59] using high-accuracy
settings for several selected flexible CoRE MOFs. At each snapshot
from the NVT simulation, one PSD calculation was performed which produces
a histogram of pore sizes. The overall PSD in a flexible material
is the cumulative histogram of individual histograms from each NVT
snapshot. A probe radius of 1.2 Å (smaller than the radius of
either Xe or Kr) was used to ensure that both open pores and narrow
constrictions are captured and can be visualized. In order to correctly
perform the ensemble average in eq , it is evident that the PSD must be converged, i.e.,
the cumulative, normalized distribution does not change with the addition
of more NVT snapshots. With the SBMOF-1 system, performing a UFF-FM
simulation of 10 ps with snapshots generated every 0.5 ps for a total
of 20 snapshots produces a nearly identical PSD to the longer simulation
procedure described previously, hence either is sufficient for performing
the ensemble average.The final PSD can then be mapped in a semiquantitative way to the Gaussian variables (σp and ⟨Rp⟩) used
in the analytical model described previously (eqs and 6). The difference
is that atoms constituting the pore wall in a real MOF are not always
carbon (as is imposed in the analytical model to allow it to be solvable)
nor are pores in real systems perfectly spherical. Therefore, some
variation between the model and direct simulations is always expected
when atoms constituting the pore walls in a given structure have different
UFF parameters and do not form a perfectly spherical shell. Thus,
the limitation of the analytical model is that it cannot be used to
directly map a computed PSD to exact values of the Henry coefficients
and selectivity for a particular MOF. In other words, it does not
replace the need to actually compute the Henry coefficient with Widom
insertions on the accumulated snapshots from the NVT simulation. However,
it does an excellent job of reproducing the trends of selectivity’s
dependence on flexibility as is seen in the following Results and Discussion section.
Results and Discussion
Intrinsic flexibility effects on Henry regime adsorption behavior
are discussed in five main points:First, the analytical model is presented
which quantitatively assesses the effects on Henry regime adsorption
of tight-fitting molecules as a function of pore flexibility.Next, the analytical model’s
results show that accounting for the systematic effects of intrinsic
flexibility are critical for the design and/or identification of the
best performing materials in this shape selective adsorption application.Next, the CoRE MOF database
is screened
using flexible models to not only validate the conclusions drawn from
the analytical model but also to demonstrate the discrepancies of
the rigid pore approximation.Next, four CoRE MOFs are selected
to specifically detail the ways in which flexibility affects a material’s
potential for Xe/Kr separation.Finally, the ideas developed thus
far are applied to the SBMOF-1 system, and we demonstrate the necessity
of using flexibility to obtain better agreement between experimental
results and computational predictions of Xe/Kr adsorption properties.
Flexibility and the Analytical Model
We have developed
both a rigid (eq ) and
flexible (eq ) pore
model to obtain insight into flexibility’s effects on Xe/Kr
Henry coefficients. The dependence of KH on the pore radius and distribution width is shown in Figure . The most interesting consequence
of flexibility is that the pore sizes resulting in the largest KH,r are the most overpredictive of KH,f and the pore sizes with smaller KH,r are the most under-predictive of KH,f. The size of these over(under-)predictions is strongly
dependent on the strength of pore size fluctuations (σp), which is shown in Figure a (Xe) and Figure b (Kr) when differing σp values are plotted.
The overpredictions occur since there exists a finite probability
that the pore deviates from the optimal size, even when the most probable
configuration is the optimal size. The under-predictions occur since
there exists a finite probability that the pore can adopt the optimal
size, even though the most probable configuration is not the optimal size. Thus, the main observation from this analysis
is that, even if relatively small fluctuations (σp < 0.4 Å) in a flexible pore average out such that ⟨Rp⟩ is equivalent to Rp in the rigid approximation, the flexible pore Henry
coefficient can differ significantly. We will see in subsequent discussions
that, similar to the green curve in Figure , σp ≈ 0.3 Å
for SBMOF-1.
Figure 2
Broadening of the flexible Henry coefficient profile, KH,f(⟨Rp⟩,
σp), is calculated for increasing values of the pore
size distribution
width, σp = {0.0, 0.07, 0.31, 1.0}, for both (a)
a Xe adsorbate and (b) a Kr adsorbate.
Broadening of the flexible Henry coefficient profile, KH,f(⟨Rp⟩,
σp), is calculated for increasing values of the pore
size distribution
width, σp = {0.0, 0.07, 0.31, 1.0}, for both (a)
a Xe adsorbate and (b) a Kr adsorbate.More interesting than just KH from
an applications perspective is the infinite dilution selectivity of
Xe/Kr, which was formulated for flexible and rigid pores in eqs and 7, respectively. The selectivity for the flexible pore model was calculated
over the bounds 2.5 Å < ⟨Rp⟩ < 10.0 and 0.0 Å < σp < 1.0
Å and mapped over this two-dimensional space, as shown in Figure . It is immediately
evident from Figure a that, since the contours are not vertical lines, the rigid pore
approximation will yield a different selectivity than a flexible pore
(i.e., when σp ≠ 0). Figure b additionally reveals extremely sharp gradients
in Sf(⟨Rp⟩, σp) when ⟨Rp⟩ is slightly smaller than the optimal size (∼4.7
Å) for Xe selectivity.
Figure 3
Selectivity of Xe to Kr mapped onto the average
pore radius (x dimension) and the distribution width
of the radius (y dimension) for the fluctuating pore
model. The color scale
in (a) is a linear scale of the flexible selectivity, Sf, whereas the color in (b) is the log10 scale
of Sf to better emphasize the gradients
that exist over small changes in ⟨Rp⟩ and σp.
Selectivity of Xe to Kr mapped onto the average
pore radius (x dimension) and the distribution width
of the radius (y dimension) for the fluctuating pore
model. The color scale
in (a) is a linear scale of the flexible selectivity, Sf, whereas the color in (b) is the log10 scale
of Sf to better emphasize the gradients
that exist over small changes in ⟨Rp⟩ and σp.There are three distinct situations where a flexible pore
can result
in significantly different predicted selectivity than a rigid pore.
First, the optimal pore for Xe selectivity in this analytical model
has ⟨Rp⟩ ≈ 4.7 Å
and σp = 0 Å. Yet fluctuations on the order
of σp ≈ 0.6 Å can reduce the selectivity
of such a pore by a factor of 2. Second, a rigid pore predicted to
be Kr selective can very easily be nonselective or even Xe selective
if the pore undergoes small fluctuations (σp ≈
0.15 Å). Third, predicted selectivity can be quite different
when flexible and rigid ⟨Rp⟩
are not equivalent. If thermal fluctuations in a flexible pore do
not average out to the same value as the rigid pore, Sr can vastly overpredict Sf. For example, if a rigid pore has Rp = 4.7 Å and overestimates the average flexible pore ⟨Rp⟩ by 0.6 Å, the rigid selectivity
could be reduced by a factor of 50. The sensitivity of adsorption
properties to small changes in pore sizes has been shown in the literature
when different DFT methods were used to optimize the crystal structure.[60−62] However, we are highlighting an entirely different situation where
the average pore size changes due to flexibility, an effect which
we will demonstrate for real MOF systems later on. Most interestingly,
the global optimum for selectivity as a function of flexibility occurs
for an entirely rigid pore. This is discussed further in the Flexibility and Optimal Separations section.
Flexibility and Optimal Separations
We have systematically
demonstrated how we expect shape selective adsorption separations
to have an intricate, nontrivial dependence on intrinsic flexibility,
having chosen the specific application of Xe/Kr separations to illustrate
our findings.Figure summarizes how this information can be exploited
for the design and prediction of better separation materials. To construct
this figure, we have extracted Sf from Figure at constant σp and normalized the x-axis of ⟨Rp⟩ by ⟨Rp⟩opt such that the optimal selectivity for
a given σp occurs at a value of 1. The global optimum
of Sf in (⟨Rp⟩,σp) space occurs when σp = 0.
Figure 4
Flexible selectivity from the analytical model is plotted
as a
function of ⟨Rp⟩ divided
by the optimal pore size, ⟨Rp⟩opt, such that the point of optimal selectivity is normalized
to 1 for all values of σp. This demonstrates that
maximizing selectivity is achieved not simply by having the optimal
pore size but also by simultaneously minimizing intrinsic flexibility.
Although, interestingly, pore sizes that are smaller than the optimal
size can have their selectivity significantly improved with increasing
flexibility.
Flexible selectivity from the analytical model is plotted
as a
function of ⟨Rp⟩ divided
by the optimal pore size, ⟨Rp⟩opt, such that the point of optimal selectivity is normalized
to 1 for all values of σp. This demonstrates that
maximizing selectivity is achieved not simply by having the optimal
pore size but also by simultaneously minimizing intrinsic flexibility.
Although, interestingly, pore sizes that are smaller than the optimal
size can have their selectivity significantly improved with increasing
flexibility.This clearly demonstrates
that designing MOFs with the optimal
combination of pore size and chemistry is not sufficient to achieve
a global optimum in performance; one must minimize
intrinsic flexibility while simultaneously realizing the optimal average
pore size to achieve the best separation. It also demonstrates that,
while fluctuations reduce the selectivity of the optimally rigid pore,
sufficiently large fluctuations expand the range of average pore sizes
(or the number of MOFs) for which flexibility can improve selectivity.
Nonetheless, the global optimum in ⟨Rp⟩ and σp space occurs for σp = 0. In other words, if one could design the perfectly optimal
rigid pore with the ideal size and chemical composition, increasing
flexibility would only lead to worse performance. These results provide
a guiding principle in the rational design of nanoporous materials
for shape selective separations and are validated when studying the
effects of flexibility on Xe/Kr adsorption in real systems, i.e.,
the CoRE MOF database, which is the focus of subsequent discussion.
Flexibility in CoRE MOF Screening
From the analytical
model it is evident that flexibility is important when a material’s
pores approach the same size as the adsorbed molecules. For a correct
screening it is therefore important to take framework flexibility
into account, and to do this, we calculate Sf with the reported CoRE MOF experimental structure as the
starting framework configuration and input for UFF-FM. Three plots
are instructive for comparison with the results from the analytical
model.First, the Henry coefficient of Xe in the flexible material
(KH,fXe) is plotted versus the corresponding rigid Henry coefficient
(KH,rXe) in Figure , and each material is color coded by their largest included sphere
(D).[59] For materials with very large D, the rigid and flexible calculations tend to give
equitable results for the Xe Henry coefficient. However, for smaller
pores and those that are the optimal size for Xe selectivity, orders
of magnitude discrepancy can exist between the calculated Henry coefficients
for the flexible structure and the rigid approximation. This discrepancy
is attributed to pore size fluctuations, slight changes in ⟨Rp⟩, or a combination of both, all of
which is clearly demonstrated by the results of the analytical model
shown in Figures and 3.
Figure 5
Flexible Xe Henry coefficient (KH,fXe) is plotted
versus the rigid
Xe Henry coefficient (KH,rXe). The color-coding of materials by
their largest included sphere shows that the rigid approximation tends
to perform worse as a material’s pore size decreases.
Flexible Xe Henry coefficient (KH,fXe) is plotted
versus the rigid
Xe Henry coefficient (KH,rXe). The color-coding of materials by
their largest included sphere shows that the rigid approximation tends
to perform worse as a material’s pore size decreases.Second, Figure plots the flexible selectivity versus the
rigid selectivity, and
data points are color coded by the material’s KH,fXe such
that the most interesting materials in terms of Xe affinity are colored
yellow. Purple colored materials by comparison are expected to have
very low infinite dilution uptake. The rigid approximation performs
decently for some structures which remain on the y = x line of parity. However, there is very noticeable
scatter, and considering flexibility can result in orders of magnitude
deviation. Among top performing structures from the entire screening, Sr almost always overestimates Sf, supporting our conclusion that rigid pores are the
globally optimal solution since, if a material already achieves the
optimal pore size for a given chemistry, fluctuations will only reduce
the selectivity. Medium performing structures tend to have both significant
over(under-)estimations, while the lowest performing rigid structures
tend to exhibit a huge underestimation of the selectivity. This systematic
dependency is visualized another way in Figure b, where the histogram shows that, among
top performing structures, simulating flexibility reduces performance
in ∼95% of materials. By contrast, for the lowest performing
MOFs, flexibility increases performance in ∼90% of the materials.
The red highlighted regions in Figure a show where the rigid and flexible simulations predict
reverse selectivity. Thus, a pore that was a good fit for Xe can become
too small (lower right region), or one that was too small can become
enlarged and favorable by intrinsic flexibility (upper left region)
and result in a material with large selectivity for Xe. This systematic
behavior has already been predicted by the solution of the analytical
model shown in Figure .
Figure 6
(a) Flexible selectivity is plotted versus rigid approximation
selectivity for screened CoRE MOFs. Highlighted regions in red demonstrate
areas where the rigid approximation and the flexible simulations predict
reverse selectivity of one another. Materials are color coded by the
log10 value of the flexible Xe Henry coefficient, KH,fXe [mol (kg Pa)−1], to highlight the best flexible
materials for Xe infinite dilution uptake. (b) A histogram view of
the same data is shown. The red histogram shows that the larger the
rigid selectivity becomes (i.e., the more optimal the pore size and
chemistry), the more frequently that flexibility actually reduces
the performance.
(a) Flexible selectivity is plotted versus rigid approximation
selectivity for screened CoRE MOFs. Highlighted regions in red demonstrate
areas where the rigid approximation and the flexible simulations predict
reverse selectivity of one another. Materials are color coded by the
log10 value of the flexible Xe Henry coefficient, KH,fXe [mol (kg Pa)−1], to highlight the best flexible
materials for Xe infinite dilution uptake. (b) A histogram view of
the same data is shown. The red histogram shows that the larger the
rigid selectivity becomes (i.e., the more optimal the pore size and
chemistry), the more frequently that flexibility actually reduces
the performance.Finally, we plot the
relative error of the rigid approximation
(Sf/Sr) in
log10 scale versus D in Figure . We observe exactly what one might expect given the results of the
analytical model. The divergence of Sf from Sr increases as the pore size decreases
and is very significant in the range of D for optimal Xe selectivity. Additionally, the analytical
model is mapped onto the screening results in Figure by converting ⟨Rp⟩ to D via eq :where Dcarbon =
3.4 Å is the van der Waals diameter of a carbon atom. The black,
red, and purple lines represent Sf/Sr for σp values of 0.005, 0.04,
and 0.35, respectively. The trend in the screening data is captured
well by the analytical model despite its simplicity in assuming all
pore wall atoms are carbon and are arranged in a perfectly spherical
shell. Superimposing the analytical model in this way also does not
account for when the flexible and rigid ⟨Rp⟩ are not identical for a particular material.
This effect, which is demonstrated in subsequent discussion, would
additionally change how the analytical model is mapped on Figure . Most importantly,
these analyses demonstrate that the screening results agree with the
analytical model: The best rigid approximation materials (which ignore
framework fluctuations) overestimate the selectivity when flexibility
is considered.
Figure 7
Relative error from the rigid structure approximation, Sf/Sr, is plotted
in log10 scale against D. Each material is color-coded by log10[Sr]. The screening results are compared to the
analytical model where the solid black, red, and purple lines represent Sf(D, σp = 0.005)/Sr(D), Sf(D, σp = 0.04)/Sr(D), and Sf(D, σp = 0.35)/Sr(D), respectively.
Relative error from the rigid structure approximation, Sf/Sr, is plotted
in log10 scale against D. Each material is color-coded by log10[Sr]. The screening results are compared to the
analytical model where the solid black, red, and purple lines represent Sf(D, σp = 0.005)/Sr(D), Sf(D, σp = 0.04)/Sr(D), and Sf(D, σp = 0.35)/Sr(D), respectively.We caution that our screening calculations were not performed using a pocket-blocking algorithm since flexibility in
points of constriction in the pore network makes the accessibility
of pockets a function of time. Instead the screening results are only
visualized for structures where KH,rXe > 1 × 10–8 mol/(kg·Pa) as an approximate way to filter out nonporous structures.
We closely investigate and explain the performance of selected structures,
for which we manually ensure that pockets of inaccessibility do not
exist, via comparison to the analytical model in the following section.
Flexibility in Selected CoRE MOFs
Several MOFs are
selected from the screening study to illustrate in greater detail
the various ways in which flexibility changes the selectivity by comparison
to the rigid structure approximation. For these structures, NVT simulations
show that the rigid pore approximation does not present a good statistical
representation of the PSD when the host framework fluctuates at room
temperature. Figure presents a visual analysis of flexibility in four selected CoRE
MOFs and demonstrates how thermal fluctuations affect the PSD and
thus the Xe/Kr selectivity. For each material we show the flexible/rigid
PSD as well as visualization of the rigid structure (left image) and
a snapshot of the flexible structure (right image) from the UFF-FM
MD run. The corresponding flexible and rigid Henry coefficients and
selectivity are summarized in Table .
Figure 8
Evolution of the PSD after NVT dynamics is shown for four
CoRE
MOFs, with the experimental structure (left image) and a snapshot
from the flexible simulation (right image). Sections (a–d)
show specific cases for which flexibility has no effect, degrades,
enhances, or reverses the Xe/Kr selectivity, respectively.
Table 1
Flexible and Rigid Henry Coefficients
and Selectivity for the Four CoRE MOFs Shown in Figure
KH,f [mol/(kg·Pa)]
KH,r [mol/(kg·Pa)]
CSD code
Xe
Kr
Xe
Kr
Sf
Sr
UVEXAV
1.0 × 10–2
3.5 × 10–4
1.1 × 10–2
3.8 × 10–4
29
29
FALQOA
2.1 × 10–3
4.5 × 10–5
1.3 × 10–2
1.6 × 10–4
47
81
GIYSAJ
8.9 × 10–4
3.0 × 10–5
1.4 × 10–3
5.3 × 10–5
30
26
AMUCOB
4.3 × 10–4
2.5 × 10–5
2.9 × 10–6
5.2 × 10–6
17
0.56
Evolution of the PSD after NVT dynamics is shown for four
CoRE
MOFs, with the experimental structure (left image) and a snapshot
from the flexible simulation (right image). Sections (a–d)
show specific cases for which flexibility has no effect, degrades,
enhances, or reverses the Xe/Kr selectivity, respectively.In Figure a, UVEXAV
(MIL-120)[63] demonstrates a situation where
the selectivity remains unaffected by flexibility. The rigid PSD reveals
two pores that are very close in size, but notably the flexible PSD
shows a continuous distribution with approximately the same mean,
resulting in unchanged KH and Sf ≈ Sr. Figure b highlights FALQOA,[64] a material for which flexibility reduces Sr. The rigid PSD demonstrates a pore that is
of very favorable size for Xe adsorption which shrinks only slightly
throughout the MD run. However, the sensitivity of the Henry coefficient
to ⟨Rp⟩ is sufficient to
lower KH,fXe by an order of magnitude and halve the selectivity
when flexibility is considered. The most complex PSD in this set of
examples is exhibited by GIYSAJ (RPF-4),[65] as shown in Figure c for which flexibility serves to slightly enhance the selectivity.
Flexible simulations show that the smallest pore can essentially be
blocked due to ring rotation and the large pore shifts to a higher
mean value. Both effects serve to decrease the Henry coefficients
in the flexible structure but in such a way as to slightly raise the
selectivity overall. AMUCOB (BioMIL-2)[66] in Figure d presents
arguably the most interesting behavior, as it is Kr selective under
the rigid pore approximation but very Xe selective when flexibility
is considered due to an overall increase in pore size. AMUCOB is just
one of several CoRE MOFs to display this phenomena as previously discussed
with Figure . Additionally,
we note that each structure’s flexible selectivity is higher
than the experimental selectivity of SBMOF-1, a material which is
the focus of discussion in the following section.
Flexibility
in SBMOF-1
The screening data and the analytical
model demonstrate that when a given material already has the optimal
pore size to maximize selectivity, increasing intrinsic pore flexibility
only serves to reduce the selectivity performance. This effect can
be shown in the context of a particular well-known Xe/Kr separations
system. Here our flexibility calculations are benchmarked against
experimental results for the highly performing Xe/Kr separation material,
SBMOF-1, to once again show that pore flexibility reduces the performance
in selectivity of optimal rigid materials. This system was chosen
since it was identified as the best performer from a high-throughput
screening study[22] but showed a large discrepancy
between experimental and computational Henry coefficients when using
the rigid pore approximation.[23] Thus, we
focus on this structure to show how consideration of framework flexibility
better aligns computations with experiments and reduces the optimal
selectivity. DFT/PBE+D3, UFF-FM, and UFF-CDM were all used to model
framework dynamics in SBMOF-1, and the resulting Henry coefficient
and selectivity calculations are summarized in Table . The rigid structure approximation of SBMOF-1
(KAXQIL) has the optimal pore size for maximizing the Xe Henry coefficient
and selectivity. However, considering flexibility reduces these quantities
and leads to better agreement with experiments. UFF-CDM generated
dynamics provide the best agreement with experiments, and there exists
a significant decrease in the Henry coefficients and selectivity when
compared to the rigid pore approximation.
Table 2
Henry Coefficients
and Selectivity
in SBMOF-1 for the Rigid Pore Approximation and Various Framework
Dynamics Methodsa
KH [mol/(kg·Pa)]
description
flexibility
Xe
Kr
SXe/Kr
experimental data
N/A
3.84 × 10–4
2.37 × 10–5
16
KAXQIL deposited structure
no
1.45 × 10–2
2.70 × 10–4
54
KAXQIL DFT optimized
no
1.03 × 10–2
2.20 × 10–4
47
AIMD (1 × 2 × 1)
yes
7.49 × 10–3
1.85 × 10–4
41
AIMD (2 × 2 ×
1)
yes
6.80 × 10–3
1.77 × 10–4
38
AIMD (1 × 3 × 1)
yes
6.68 × 10–3
1.72 × 10–4
39
UFF-FM
yes
6.24 × 10–3
1.67 × 10–4
37
UFF-CDM
yes
3.18 × 10–3
1.28 × 10–4
25
The “Description”
column gives the simulation type (and number of unit cell replications
used in the AIMD simulation), and the “Flexibility”
column denotes a flexible simulation. Experimental data from ref (23) is included.
The “Description”
column gives the simulation type (and number of unit cell replications
used in the AIMD simulation), and the “Flexibility”
column denotes a flexible simulation. Experimental data from ref (23) is included.This decrease in Henry coefficients
fundamentally arises from thermal
disordering in SBMOF-1, visualized in Figure . The impact of flexibility on the PSD for
each dynamics method is quantitatively shown in Figure . While the rigid pores are
of optimal size for maximizing selectivity, the existence of flexibility
in all cases leads to pore size fluctuations and a shrinking of average
pore size away from its optimal value. As predicted by the analytical
model, both effects can serve to reduce the Henry coefficients (of
both Xe and Kr) and the overall selectivity of the material.
Figure 9
DFT optimized
cell (replicated 3 × 6 × 2) is depicted
on the left, while a snapshot from a MD trajectory generated with
UFF-CDM is depicted on the right. Thermal disordering of the structure
results in a change in the PSD accessible to Xe/Kr adsorbates.
Figure 10
Evolution of the PSD is shown from the
rigid structure (red histogram)
to the flexible structure (green histogram). (a–c) PSD for
1 × 2 × 1, 2 × 2 × 1, and 1 × 3 × 1
AIMD, respectively, where the rigid structure corresponds to the DFT
minimized framework. (d) PSD for UFF-FM with the rigid structure corresponding
to the KAXQIL experimentally resolved framework. and (e) PSD for UFF-CDM
where the rigid structure is the DFT minimized framework.
DFT optimized
cell (replicated 3 × 6 × 2) is depicted
on the left, while a snapshot from a MD trajectory generated with
UFF-CDM is depicted on the right. Thermal disordering of the structure
results in a change in the PSD accessible to Xe/Kr adsorbates.Evolution of the PSD is shown from the
rigid structure (red histogram)
to the flexible structure (green histogram). (a–c) PSD for
1 × 2 × 1, 2 × 2 × 1, and 1 × 3 × 1
AIMD, respectively, where the rigid structure corresponds to the DFT
minimized framework. (d) PSD for UFF-FM with the rigid structure corresponding
to the KAXQIL experimentally resolved framework. and (e) PSD for UFF-CDM
where the rigid structure is the DFT minimized framework.For DFT/PBE+D3, only a small number of unit cell
replications is
computationally feasible. Interestingly, 1 × 2 × 1, 2 ×
2 × 1, and 1 × 3 × 1 simulations all display different
PSDs, suggesting that the flexibly determined PSD can be system size
dependent, since the system is simply too constrained when considering
only one and two replications in certain crystallographic directions.
Similar finite size effects have recently been reported where multiple
unit cell replications were necessary to observe crystallographic
deformations.[16] However, the key feature
is that the mean pore size always decreases leading to reduced Henry
coefficients of both adsorbates, which is accompanied by a reduction
in the selectivity. The identical trend is observed in the larger
classical simulations. Thus, a major finding from this analysis is
that, for all flexible simulation methods, the thermodynamic fluctuations do not average out to the rigid pore approximation. Different
methods (classical vs ab initio) for host framework
dynamics yield similar evolution of the PSD’s from the rigid
to flexible simulations, and the computed KH,f is always in better agreement with experiments due to the decrease
in ⟨Rp⟩.It should
be noted that the nonbonded parameters for guest–framework
interactions also have an effect on the predicted Henry coefficients
and selectivity. We find that the Boato and UFF parameters for guest–framework
interactions do not perfectly replicate the DFT/PBE+D3 potential energy
surface, which is shown in the SI. Regardless,
the data presented here show the large dependence of the adsorption
properties on flexibly induced changes in the pore size.
Conclusions
The chemical tunability of MOFs is constantly exploited to create
adsorption sites with a high selectivity. However, in the case of
shape selective adsorption separations where the pore size and shape
are commensurate with similarly sized adsorbates like Xe/Kr, the efficiency
of these adsorption sites for separations relies on subtle geometric
differences, which we have shown to be strongly influenced by flexibility.
In this work we have systematically addressed the nontrivial dependence
of selectivity on intrinsic flexibility, providing a comprehensive
outlook for the design and/or identification of optimal shape selective
separation materials in the context of Xe/Kr mixtures. Quantification
of the effect of flexibility on the separation of Xe/Kr mixtures using
an analytical model and molecular simulations shows that some materials’
selectivity can be increased, while others’ decreased by flexibility.
However, for those materials already displaying the optimal pore size
for a given pore chemistry, increasing pore size fluctuations serve
only to further decrease selectivity. Hence the design of a globally optimal separation must not only focus on optimizing
pore size and chemistry but also on minimizing intrinsic flexibility.
From an experimental design point of view, one must simultaneously
aim for MOFs with ligands, coordination environments, and topologies
that constitute the most rigid framework possible and the optimal pore size and chemistry to achieve maximum possible
selectivity.An equally important part of this work discusses
the validity of
the rigid framework approximation in shape selective adsorption applications.
In most computational high-throughput screening studies, the MOF structure
is assumed to be rigid for computational efficiency reasons, and we
investigated whether this assumption has biased the selection of optimal
materials. Our results show that, among the top performing structures
in the rigid framework approximation, simulations accounting for flexibility
lead to a reduction of selectivity in ∼95% of these materials.
Conversely, this screening also demonstrated that fluctuations alone
can cause a material to reverse its selectivity when the average pore
size is less than the optimal value for Xe adsorption. Among the lowest
performing structures in the rigid framework approximation, ∼90%
of these materials had their selectivity increased when accounting
for framework flexibility. These results suggest that flexibility
should be considered in shape selective screening studies for the
highest degree of accuracy possible and to achieve the best ranking
of high-performance materials.SBMOF-1, which was recently crowned
as the material with the highest
Xe/Kr selectivity from a computational screening of rigid MOFs, was
re-evaluated with flexibility using both ab initio and classical MD calculations. This resulted in better agreement
with experimental data. Naturally the question then arises if there
are materials which can be experimentally demonstrated to have better
Xe/Kr selectivity than SBMOF-1. We have presented four structures
(CSD reference codes UVEXAV, FALQOA, GIYSAJ, and AMUCOB) identified
in our screening study whose predicted Sf is higher than the experimental selectivity of SBMOF-1 and used
each structure’s PSD evolution in NVT simulations to observe
how flexibility affects Xe and Kr Henry regime uptake. Through a variety
of MD methods, we demonstrated that flexibility always serves to reduce
the Henry coefficients of Xe and Kr and selectivity in SBMOF-1, bringing
better alignment between experimental results and computational predictions
for this material’s adsorption properties.The concepts
developed in this work can now be applied to other
shape selective separations. Such an example would be CO2/CH4 separations where, like Xe/Kr mixtures, the kinetic
diameters of both adsorbates are of similar size. Here one would expect
intrinsic flexibility to affect the Henry regime selectivity as well.
Similar to Xe/Kr separations, there would exist an optimal pore size
and chemistry that maximizes the rigid selectivity for one of the
adsorbates, but the more flexible this optimal pore is, the more the
selectivity will be reduced. And while our analytical model only accounts
for isotropic pore deformations, it would also be useful to develop
another model in which an additional flexibility parameter characterizes
the degree of anisotropy of the pore deformation since CH4 is an isotropic particle but CO2 is not. This development
of more intricate analytical models in conjunction with a similar
screening of flexible CoRE MOFs could lead to new insights regarding
the usefulness of MOFs for CO2/CH4 separations.Finally, we re-emphasize that we have focused on predicting Henry
regime selectivity. However, both the analytical model and the flexible
screening methods could be extended to obtain selectivity at higher
pressures with additional assumptions and more computational cost,
respectively. In the cases of higher pressure, the adsorption behavior
will then depend on the exact potential energy profile of the host
as a function of the pore size, since less energetically favorable
conformations of the framework can be stabilized with increasing chemical
potential. Thus, it is likely that new insights will be obtained for
the selectivity dependence at higher pressures. Such future work will
have two major benefits. First, we will understand if the trends observed
in this work between flexibility and separation performance hold at
high pressure (where many separations are performed). Second, we will
be able to determine over what pressure ranges Henry’s law
is applicable in flexible materials and whether it differs from the
Henry regime pressure range in the rigid pore approximation.
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