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This article is part of the
Metal-organic frameworks web themed issue
Guest editors: Neil Champness, Christian Serre and Seth Cohen
All articles in this issue will be gathered together
online at www.rsc.org/metal-organic-frameworks
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View Article Online / Journal Homepage / Table of Contents for this issue
10496 Chem. Commun., 2012, 48, 10496–10498 This journal is c The Royal Society of Chemistry 2012
Cite this: Chem. Commun., 2012, 48, 10496–10498
Understanding excess uptake maxima for hydrogen adsorption isotherms
in frameworks with rht topologywzDavid Fairen-Jimenez,ya Yamil J. Colon,ya Omar K. Farha,
bYoun-Sang Bae,
ac
Joseph T. Huppband Randall Q. Snurr*
a
Received 6th August 2012, Accepted 6th September 2012
DOI: 10.1039/c2cc35711a
For a series of metal–organic frameworks with rht topology, we study
computationally the effect of the linker length on the surface area,
pore size, and pore volume, relating them with the hydrogen adsorp-
tion properties. The results provide new insights about the excess
capacities and the pressures where the uptake maxima in the excess
isotherms occur. We found that, of the materials studied, NU-109/L7
has the optimal pore volume for excess gravimetric hydrogen uptake.
The development of new porous materials for adsorption
applications has turned increasingly to metal–organic frame-
works (MOFs) due to their structural diversity and the resulting
functionality. MOFs are obtained by the self-assembly of metal
clusters and organic linkers, resulting in tailored nanoporous
host materials. MOFs show great promise in many areas,
including industrial gas separation and storage. In particular,
hydrogen storage has received much attention.1 NewMOFs are
being synthesised at a very fast pace today, and for many
materials, hydrogen adsorption is one of the first properties
to be characterised. The high internal surface areas and large
pore volumes make MOFs promising candidates for hydrogen
storage, especially at cryogenic temperatures.2
Efforts to increase the surface area and pore volume of
MOFs have often focused on increasing the length of the organic
linkers. However, the possibility of catenation increases significantly
when using long linkers.3 Network catenation occurs when two or
more independent, identical networks are entangled, partially filling
each other’s pores, and cannot be separated without breaking
bonds. Catenation has been a major concern in the design of
low-density porous structures since it significantly reduces the
pore size and volume. In the last few years, several MOFs with
very large pore volumes and surface areas have been synthesized
using topologies that prevent the possibility of catenation.4–10
Among these materials, we focus here on a series of isoreti-
cular MOFs with (3,24)-paddlewheel-connected networks and
rht-topology, used independently by the groups of Eddaoudi,4
Schroder,5 Zaworotko,6 Zhou,7 and us.8 The rht topology can
be described as having either three or four cages, depending
on whether the curvature of the linkers is taken into account
(Fig. S3 and S4, ESIz).11 These structures share a common
cavity (yellow sphere in Fig. S3 and S4, ESIz) which is enclosed
by the copper paddle wheel corners and the R2 portion of
the linker (Scheme 1) and is, thus, almost independent of the
linker length. In this work, we study computationally the
influence of the linker length on the pore volume, pore size,
surface area, and hydrogen adsorption. We focus particular
attention on the hydrogen capacity and the pressures at which
the maxima in the excess adsorption isotherms occur. We then
compare our simulations with available experimental data and
propose new guidelines for the validation of future results.
Our strategy to build the different structural models is similar
to the scheme we followed in a previous paper.8 We start with
the asymmetric unit ofNOTT-112, synthesized by Schroder and
co-workers.5 We maintain the same copper paddlewheel cluster,
the Fm3m group symmetry, and the rht network topology, but
we substitute the organic linker. Scheme 1 shows the hexa-
protonated precursor of the original NOTT-112 linker and the
Scheme 1 (a) Hexa-protonated precursor of the linker used to construct
the L1–L8 isostructural materials, and (b) the Lx linker fragments.
aDepartment of Chemical & Biological Engineering, NorthwesternUniversity, 2145 Sheridan Road, Evanston, Illinois 60208-3120,USA. E-mail: [email protected]; Tel: +1-847-467-2977
bDepartment of Chemistry and International Institute forNanotechnology, Northwestern University, USA
cDepartment of Chemical and Biomolecular Engineering, YonseiUniversity, 262 Seongsanno, Seodaemun-gu Seoul 120-749, S. Koreaw This article is part of the ChemComm ‘Metal–organic frameworks’web themed issue.z Electronic supplementary information (ESI) available: Simulationprocedures, structural information and adsorption data. See DOI:10.1039/c2cc35711ay These authors contributed equally.
ChemComm Dynamic Article Links
www.rsc.org/chemcomm COMMUNICATION
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This journal is c The Royal Society of Chemistry 2012 Chem. Commun., 2012, 48, 10496–10498 10497
new variants we used to build a series of isoreticular MOFs,
where some of these materials have been already synthesised: L1
(PCN-61),7 L2 (NU-111),11 L3 (NOTT-112),5 L4 (NOTT-119/
PCN-69),7,10 L5 (NOTT-116/PCN-68),7,9 L6 (PCN-610/
NU-100)7,12 and L7 (NU-109).13 After the asymmetric unit is
modified, the symmetry operations of the space group allow
the construction of the new structure. The unit cell was then
subject to geometry optimisation based on molecular mechanics,
modifying the size of the unit cell and the atomic coordinates
of the new structure.
The energy minimisations produced eight structures, named
here L1�L8, with cubic unit cell lengths in the range of 43 to
68 A. We performed grand canonical Monte Carlo (GCMC)
simulations on these structures to predict the H2 adsorption
isotherms at 77 K. It is important to note that simulations calculate
the absolute amount of gas adsorbed, NAbs, while experiments
measure the excess adsorption, NExc. These quantities are
related by:
NExc = NAbs � rVpore (1)
where r is the density of the bulk gas (i.e. hydrogen) at the
adsorption pressure and temperature, and Vpore is the pore
volume of the adsorbent. A popular way to estimate the bulk
density is using the Peng–Robinson (PR) equation of state
(EOS).14 Fig. S5 (ESIz) compares the density of hydrogen as a
function of pressure calculated with PR and the experimental
density obtained from the National Institute of Standards and
Technology (NIST).15 The densities match well, but with some
deviations at higher pressures. We focus here on results using
the NIST H2 density data to convert between excess and
absolute isotherms.
We first validated our results by comparing the simulated
isotherms at 77 K on L2 with experimental isotherms on the
analogous structure NU-111. Fig. 1 shows that the simulations
accurately predict the experimental absolute isotherm, calculated
using the H2 bulk density provided by NIST, across all pressures.
For the excess isotherms, the simulations also agree well with
experiment and correctly describe the location of the adsorption
maximum at ca. 40.6 bar when using the NIST data. There are
only small differences at high pressures (ca. > 40 bar) when
using PR due to a small overprediction of the true H2 bulk
density (Fig. S6, ESIz).
Fig. 2a and Fig. S7 (ESIz) present the gravimetric and
volumetric, excess and absolute adsorption isotherms on the
different materials. Tabulated data are available in the ESIz;Table S2 summarizes the main results. On a gravimetric basis,
structure L8 exhibits the highest absolute hydrogen uptake,
whereas L7 has the highest excess hydrogen uptake. It should
be noted that although L8 possesses the largest pore volume,
cavity size, and surface area, it does not exhibit the highest
uptake in terms of excess. This can be explained by eqn (1).
For L8, the large pore volume reduces the excess uptake.
Fig. 2b further illustrates this concept. While larger pore
volume increases the absolute uptake, there is an optimum
pore volume for the excess uptake, which corresponds to
3.61 cm3 g�1 (NU-109/L7). For hydrogen storage applications,
the volumetric capacity is also of great importance, especially for
transportation applications, where the volume of the reservoir is
limited. In terms of volumetric capacity, it is remarkable that the
material ranking inverts, with L1 (34.98 mg cm�3) showing the
highest uptake and L8 (17.92 mg cm�3), the lowest (Fig. S7, ESIz).The relation between the pressure where the maximum
gravimetric excess is found and the different textural proper-
ties of the materials is illustrated in Fig. 3 and Fig. S8 (ESIz).Excess maxima are located in the range 33.1–51.5 bar, corres-
ponding to L1 (shortest linker) and L8 (longest linker),
respectively. There is a clear relation between these maxima
and the corresponding geometrical surface area (Fig. 3), unit
cell size and pore volume (Fig. S8, ESIz). The pressures of theexcess maxima are also correlated with the sizes of the larger
cavities of the rht topology, but not with the common cavity
Fig. 1 Absolute (diamonds) and excess (triangles) H2 adsorption
isotherms at 77 K. Simulations (red) were performed in L2,
and experiments (black) were performed on its analogue, NU-111.11
Bulk hydrogen densities required in eqn (1) were calculated using
NIST data.
Fig. 2 (a) Calculated excess adsorption isotherms for H2 at 77 K on the
materials L1–L8, and (b) calculated absolute (black circles) and excess (red
circles) adsorption capacity maxima of H2 isotherms on L1–L8 obtained at
77 K. The H2 bulk density was obtained from the NIST data.
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10498 Chem. Commun., 2012, 48, 10496–10498 This journal is c The Royal Society of Chemistry 2012
that is defined by the copper paddle-wheels. It seems obvious
that, in the absence of catenation, an increase in the linker length
implies an enlargement of the pore size, the pore volume, the
surface area and the absolute H2 capacity. The size of the linker
and therefore the pore volume affect, in turn, not only the
number of molecules that can adsorb in the material, but also
the relation between absolute and excess amounts (eqn (1)).
Finally, we compared our simulations on L5 with available
experimental data from the Schroder, NOTT-116,9 and Zhou,
PCN-68,7 groups. As shown in Fig. S9 (ESIz), the experimental
hydrogen adsorption isotherms for the nominally composition-
ally identical NOTT-116 and PCN-68 are generally similar, but
the pressures where the maxima in the excess isotherms occur are
ca. 30 and 46 bar, respectively. Moreover, after reaching the
maximum in the excess isotherm, the amount adsorbed decreases
much faster in NOTT-116 than in PCN-68. From Fig. 3, we
can observe that some experimental data in rht MOFs follow
the expected trend. Deviations from this trend might be related
to experimental challenges in the adsorption measurements
(e.g. instrumental calibration issues related to assessment of empty
reactor, manifold and dead volumes, thermal transpiration, etc.),
or they might reflect difficulties in sample activation.16
In this work we have shown, using computational methods,
the effect of linker length on the textural properties of rht-type
MOFs such as surface area, pore size, and pore volume and
their relation to hydrogen adsorption properties. We showed
that although absolute uptake capacity increases linearly with pore
volume, excess uptake capacity maximizes at a pore volume of
ca. 3.61 cm3 g�1 (L7/NU-109). Further increases in pore volume
and pore size increase the pressure at which the maximum occurs,
but not the excess uptake capacity. We predicted the pressure at
which the excess maximum occurs as a function of the textural
properties of the structures. We believe that these relationships
will serve as guides for the synthesis of novel materials with
the rht topology and for understanding their hydrogen
uptake. We further suggest that gross ‘‘real world’’ deviations
from computationally observed trends could be indicative of
experimental issues, and thus may prove to be an instructive,
corroborative, or (alternatively) usefully critical, diagnostic of
experimental findings for yet-to-be-developed high-hydrogen-
capacity metal–organic framework materials.
This work was funded by the Department of Energy’s Office
of Energy Efficiency and Renewable Energy, Fuel Cell Technol-
ogies Program under Grant DE-FC36-08GO18137 and as a
cooperation project No. KK-1201-F0 (Synthesis of Porous
Hybrids and Their Applications) and supported by the Korea
Research Institute of Chemical Technology (KRICT). YJC
thanks the National Science Foundation Graduate Research
Fellowship Program. Computational work was supported
through resources provided by Information Technology at
Northwestern University as part of its shared cluster program,
Quest (p20320), and by the National Energy Research Scientific
Computing Center.
Notes and references
1 M. P. Suh, H. J. Park, T. K. Prasad and D.-W. Lim, Chem. Rev.,2011, 112, 782–835.
2 H. Furukawa, N. Ko, Y. B. Go, N. Aratani, S. B. Choi, E. Choi,A. O. Yazaydin, R. Q. Snurr, M. O’Keeffe, J. Kim andO. M. Yaghi, Science, 2010, 329, 424–428.
3 N. L. Rosi, M. Eddaoudi, J. Kim, M. O’Keeffe and O. M. Yaghi,Angew. Chem., Int. Ed., 2002, 41, 284–287.
4 F. Nouar, J. F. Eubank, T. Bousquet, L. Wojtas, M. J. Zaworotkoand M. Eddaoudi, J. Am. Chem. Soc., 2008, 130, 1833–1835.
5 Y. Yan, X. Lin, S. Yang, A. J. Blake, A. Dailly, N. R. Champness,P. Hubberstey and M. Schroder, Chem. Commun., 2009, 1025–1027.
6 B. Zheng, J. Bai, J. Duan, L. Wojtas and M. J. Zaworotko, J. Am.Chem. Soc., 2010, 133, 748–751.
7 D. Yuan, D. Zhao, D. Sun and H.-C. Zhou, Angew. Chem., Int.Ed., 2010, 49, 5357–5361.
8 O. K. Farha, A. O. Yazaydın, I. Eryazici, C. D. Malliakas,B. G. Hauser, M. G. Kanatzidis, S. T. Nguyen, R. Q. Snurr andJ. T. Hupp, Nat. Chem., 2010, 2, 944–948.
9 Y. Yan, I. Telepeni, S. Yang, X. Lin, W. Kockelmann, A. Dailly,A. J. Blake, W. Lewis, G. S. Walker, D. R. Allan, S. A. Barnett,N. R. Champness and M. Schroder, J. Am. Chem. Soc., 2010, 132,4092–4094.
10 Y. Yan, S. Yang, A. J. Blake, W. Lewis, E. Poirier, S. A. Barnett,N. R. Champness and M. Schroder, Chem. Commun., 2011, 47,9995–9997.
11 O. K. Farha, C. E. Wilmer, I. Eryazici, B. G. Hauser, P. A. Parilla,K. O’Neill, A. A. Sarjeant, S. T. Nguyen, R. Q. Snurr andJ. T. Hupp, J. Am. Chem. Soc., 2012, 134, 9860–9863.
12 O. K. Farha, A. O. Yazaydin, I. Eryazici, C. D. Malliakas,B. G. Hauser, M. G. Kanatzidis, S. T. Nguyen, R. Q. Snurr andJ. T. Hupp, Nat. Chem., 2010, 2, 944–948.
13 O. K. Farha, I. Eryazici, N. C. Jeong, B. G. Hauser, C. E. Wilmer,A. A. Sarjeant, R. Q. Snurr, S. T. Nguyen, A. O. Yazaydin andJ. T. Hupp, J. Am. Chem. Soc., DOI: 10.1021/ja3055639.
14 R. C. Reid, J. M. Prausnitz and B. E. Poling, The Properties ofGases and Liquids, McGraw-Hill, New York, 4th edn, 1987.
15 E. W. Lemmon, M. O.McLinden and D. G. Friend, ‘‘ThermophysicalProperties of Fluid Systems’’, in NIST Chemistry WebBook, NISTStandard Reference Database Number 69, ed. P. J. Linstrom andW. G. Mallard, National Institute of Standards and Technology,Gaithersburg, MD, p. 20899, http://webbook.nist.gov, (July 10, 2012).
16 C. Zlotea, P. Moretto and T. Steriotis, Int. J. Hydrogen Energy,2009, 34, 3044–3057.
Fig. 3 Pressures corresponding to the maxima in the gravimetric excess
adsorption isotherms of L1–L8 at 77 K as a function of the geometrical
surface areas. Experimental data from PCN-68, red triangle, NOTT-116,
purple diamond, and NU-111, green square, are also included. The bulk
H2 density was obtained from the NIST data.
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