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. 2022 Apr 27;61(25):e202203575. doi: 10.1002/anie.202203575

Computational Identification and Experimental Demonstration of High‐Performance Methane Sorbents

Karabi Nath 1,+, Alauddin Ahmed 2,3,+, Donald J Siegel 2,3,4,, Adam J Matzger 1,
PMCID: PMC9322563  PMID: 35478372

Abstract

Remarkable methane uptake is demonstrated experimentally in three metal‐organic frameworks (MOFs) identified by computational screening: UTSA‐76, UMCM‐152 and DUT‐23‐Cu. These MOFs outperform the benchmark sorbent, HKUST‐1, both volumetrically and gravimetrically, under a pressure swing of 80 to 5 bar at 298 K. Although high uptake at elevated pressure is critical for achieving this performance, a low density of high‐affinity sites (coordinatively unsaturated metal centers) also contributes to a more complete release of stored gas at low pressure. The identification of these MOFs facilitates the efficient storage of natural gas via adsorption and provides further evidence of the utility of computational screening in identifying overlooked sorbents.

Keywords: Computational Screening, Deliverable Capacity, Interatomic Potentials, Metal Organic Framework (MOF), Methane Storage


Promising MOFs were identified computationally and experimentally demonstrate remarkable methane uptake that outperforms known benchmarks both volumetrically and gravimetrically. An advanced set of interatomic potentials that explicitly account for the presence of coordinatively unsaturated sites (CUS) in MOFs were used to identify the high‐capacity MOFs that were previously overlooked due to the limitation of the general interatomic potentials.

graphic file with name ANIE-61-0-g002.jpg


Natural gas (NG) is often cited as an important stepping‐stone in the transition to low‐carbon transportation fuels.[ 1 , 2 ] NG, comprising methane as the primary component, is an attractive gasoline alternative on account of its wide availability, established distribution network, high hydrogen to carbon ratio, and moderate carbon emissions. However, the low density of NG presents challenges for its storage that limit energy density and impede broad deployment in mobile applications such as vehicles. Particularly, the volumetric energy density of NG, which impacts the driving range of a vehicle, is much lower than that of gasoline: uncompressed NG has an energy density of 0.04 MJ L−1 while gasoline exhibits a value of 32.4 MJ L−1. [3] Physical approaches to improve volumetric storage density include liquefaction at low temperatures (∼110 K, liquefied natural gas, LNG with an energy density of ∼22.2 MJ L−1) or compression at high pressures (∼250 bar, CNG, compressed natural gas with an energy density of ∼9 MJ L−1). [4] CNG requires the use of bulky and expensive fuel tanks, and multistage compressors. [5] LNG allows for lower pressures but with the drawback of complex tank designs and pressure buildup upon extended storage. [6] Adsorbed natural gas (ANG) is a promising alternative to compression and liquefaction. [7] Adsorbents can potentially store NG at high densities at modest pressures (∼35–80 bar), which translates to less costly tank designs.

MOFs with high porosity, high surface area, and tunability in structure have emerged as promising materials for ANG.[ 8 , 9 , 10 , 11 , 12 , 13 ] The most common proxy for ANG performance is methane storage capacity. For vehicular applications, a suitable adsorbent should exhibit a combination of high methane uptake at the maximum (filled state) storage pressure (65 or 80 bar)[ 14 , 15 ] with low uptake at the minimum desorption pressure (5 bar), resulting in a high usable capacity (residual gas stored at pressures below 5 bar is insufficient to power an internal combustion engine).[ 9 , 13 ] The usable (or deliverable) uptake should be distinguished from total uptake. The former is a practical metric of performance, whereas the latter represents the maximum gas stored at high pressure and does not account for any residual gas present at low pressures.

Among the many possible MOFs, HKUST‐1 is commonly cited as a benchmark methane adsorbent, given its high total methane capacity [267 cm3 (STP) cm−3 at 65 bar and 272 cm3 (STP) cm−3 at 80 bar] and excellent deliverable capacity [190 cm3 (STP) cm−3 (65–5 bar) and 200 cm3 (STP) cm−3 (80–5 bar)].[ 13 , 16 ] Tens of thousands of MOFs have been synthesized, yet only a fraction have been examined experimentally as methane sorbents due to the time‐consuming nature of these measurements. Therefore, computational screening has emerged as a useful tool for finding optimal MOFs for ANG.[ 17 , 18 , 19 , 20 , 21 , 22 , 23 , 24 , 25 , 26 ] Here, high‐throughput Grand Canonical Monte Carlo (GCMC) simulations are used to identify promising MOFs whose capacities for methane uptake exceeds that of state‐of‐the‐art materials. Experimental synthesis and methane uptake measurements reveal that three of these MOFs—UTSA‐76, UMCM‐152 and DUT‐23‐Cu—surpass the methane capacity of HKUST‐1 as well as for other noteworthy methane sorbents (Table S6), providing a new high‐water mark for methane storage materials. [27] An additional distinguishing feature of this work is the use of interatomic potentials that explicitly account for the presence of coordinatively unsaturated sites (CUS).[ 28 , 29 , 30 ] CUS MOFs used in our calculations were identified by the CoRE 2019 database based on a python code developed by Haldoupis (GitHubEmmhald/Open_metal_detector, n.d.). Figure 1 shows the predicted usable CH4 capacities for 11 185 MOFs from the CoRE [31] (2019) database at 298 K calculated using GCMC. The database includes MOFs with and without CUS. Initial screening was performed with the DREIDING(MOF)/TraPPE(CH4)[ 32 , 33 ] potential for non‐CUS MOFs and with a potential that accounts for CH4‐CUS interactions. [28] These data are shown in Figure 1. Subsequently, a portion of this data set was re‐evaluated with an additional set of interatomic potentials: UFF(MOF)/TraPPE(CH4)[ 32 , 34 ] for non‐CUS MOFs and UFF(MOF)/9‐site(CH4)[ 29 , 30 , 34 ] for CUS MOFs.

Figure 1.

Figure 1

Usable volumetric capacity of CUS and non‐CUS MOFs as a function of gravimetric capacity at 298 K under pressure swing between a) 5 and 65 bar and b) 5 and 80 bar.

In contrast to previous studies, two separate sets of interatomic potential parameters were used for CUS and non‐CUS MOFs to identify high‐capacity materials that were previously overlooked due to limitations of general interatomic potentials (Table S1). Notably, very few studies employ both computational and experimental approaches to demonstrate record‐setting MOFs. [27] The potentials used here yielded superior agreement with the experimentally measured isotherms of the MOFs, as shown in Table 1. Two isothermal “pressure swing” operating conditions at 298 K are considered: a swing between 65 and 5 bar, and between 80 and 5 bar. From these calculations, 95 CUS MOFs are predicted to surpass both usable volumetric and gravimetric CH4 capacities of HKUST‐1[ 13 , 16 ] (190 cm3 (STP) cm−3 and 0.154 g g−1) for a pressure swing between 65 and 5 bar while 96 CUS MOFs outperform HKUST‐1[ 13 , 16 , 35 ] (200 cm3 (STP) cm−3 and 0.162 g g−1) for a pressure swing of 80 to 5 bar (Tables S2 and S3). A total of only 8 non‐CUS MOFs were predicted to surpass HKUST‐1 (Tables S4 and S5). UMCM‐152 and DUT‐23‐Cu were identified as sorbents with the potential to exceed the performance of HKUST‐1.[ 36 , 37 ] These MOFs were chosen based on their predicted high performance and synthetic accessibility. In addition, UTSA‐76 was evaluated as a second benchmark material because it has been reported to outperform HKUST‐1 in the pressure range of 5–65 bar. [38] Computational predictions are based on idealized MOF models that typically assume that all solvent, un‐reacted salt, and disorder have been removed from the crystal structure. As these components can play a role in stabilizing some MOFs there is no guarantee that a given MOF can be realized experimentally in its fully activated form. In fact, a previous study [39] of hydrogen sorbents found that many promising MOFs identified from screening databases of experimentally‐known MOFs were not possible to synthesize with surface areas close to the predicted values due to various modes of collapse[ 40 , 41 ] or inadequate activation.[ 42 , 43 ] Therefore, experimental validation of predicted hits is critical.

Table 1.

Usable CH4 capacities and crystallographic properties of high‐capacity MOFs.

MOFs

CUS density[b] [mmoles g−1]

Gravimetric surface area [m2 g−1] Expt./Calc.

Pore Volume [cm3 g−1] Expt./Calc.

Pressure swing 65 to 5 bar at 298 K

Pressure swing 80 to 5 bar at 298 K

Gravimetric capacity [g g−1] Expt./Calc.

Volumetric capacity [cm3 (STP) cm−3] Expt./Calc.

Gravimetric capacity [g g−1] Expt./Calc.

Volumetric capacity [cm3 (STP) cm−3] Expt./Calc.

HKUST‐1[a]

4.96

1850/2159

0.78/0.81

0.154/0.150

190/184

0.162/0.158

200/195

UTSA‐76 (this work)

3.77

2700/3205

1.09/1.08

0.200/0.194

195/189

0.215/0.207

210/201

UMCM‐152 (this work)

3.13

3430/3480

1.45/1.38

0.247/0.259

207/205

0.271/0.276

226/219

DUT‐23‐Cu (this work)

N/A

5300/4636

2.23/1.99

0.332/0.333

190/192

0.377/0.361

216/208

[a] Usable capacities of HKUST‐1 under 65/5 and 80/5 bar pressure swing were collected from Ref. [13, 16] respectively. Measured crystallographic properties of HKUST‐1 were collected from Ref. [16]. [b] CUS density of MOFs was calculated based on the crystallographic information files.

UTSA‐76 (Figure 2a) is a CUS MOF, synthesized from a tetracarboxylate pyrimidine linker (5,5′‐(pyrimidine‐2,5‐diyl) diisophthalic acid) that exhibits a BET surface area of 2700 m2 g−1 and pore volume of 1.09 cm3 g−1 (at P/P 0=0.95) (Table 1 and Figure S9). UTSA‐76 demonstrates total volumetric (TV) uptake of 251 cm3 (STP) cm−3 at a pressure of 65 bar (298 K, Table 1) in accord with previous observations. [38] Improved capacity is achieved at 80 bar (266 cm3 (STP) cm−3) signaling that saturation had not been achieved previously. These TV values are lower than HKUST‐1 for both maximum pressures. However, UTSA‐76 exhibits significantly improved usable volumetric (UV) capacity of 210 cm3 (STP) cm−3 (80–5 bar) in comparison to HKUST‐1 (200 cm3 (STP) cm−3). The undesirable higher uptake of HKUST‐1 relative to UTSA‐76 in the 0–5 bar region is ascribed to the presence of a higher density of CUS in HKUST‐1, resulting in a larger density of methane molecules adsorbed at low pressures. [44] This observation is consistent with previous reports that the presence of CUS can have detrimental effects on the usable capacities of MOFs.[ 45 , 46 ]

Figure 2.

Figure 2

Crystal structures of MOFs being assessed for methane uptake in the present study.

UMCM‐152 (Figure 2b) is assembled from CuII paddlewheel clusters connected through tetracarboxylated triphenyl benzene linkers (5′‐(4‐carboxyphenyl)‐[1,1′ : 3′,1′′‐terphenyl]‐3,4′′,5‐tricarboxylic acid) and has a smaller CUS density relative to UTSA‐76 (Table 1). The linker has a trapezoidal geometry and two types of carboxylates: [36] one from the isophthalate group and the other is a para‐benzoate unit. The structure is composed of two cages (pore diameters: ≈16.9 and 18.6 Å). One of the cages is formed from the faces of six linker molecules and twelve CuII paddlewheel clusters while the other cage is defined by the edges of twelve linkers and six CuII paddlewheels. These cages stack in an alternate fashion. DUT‐23‐Cu (Figure 2c), on the other hand is a non‐CUS MOF composed of dodecahedral mesoporous cages with pto‐like topology, constructed from CuII and mixed linkers (4,4′‐bypyridine and H3BTB (1,3,5‐tris(4‐carboxyphenyl)benzene)).The dative ligands fully cap the copper paddlewheels blocking guest access to the metal sites. [37] The measured BET surface areas are 3430 m2 g−1 (UMCM‐152) and 5300 m2 g−1 (DUT‐23‐Cu), with pore volumes (at P/P 0=0.95) of 1.45 cm3 g−1 and 2.23 cm3 g−1 respectively (Table 1 and Figure S10 and S11).

As predicted computationally, UMCM‐152 exhibits remarkably high usable methane capacity that outperforms both HKUST‐1 and UTSA‐76, Table 1. The UV capacity of UMCM‐152 is 207 cm3 (STP) cm−3 (9 % greater than HKUST‐1 and 6 % greater than UTSA‐76) and 226 cm3 (STP) cm−3 (13 % > HKUST‐1; 7 % > UTSA‐76) under 65–5 bar and 80–5 bar pressure swings, respectively, at 298 K. On the other hand, DUT‐23‐Cu exhibits a UV capacity of 190 cm3 (STP) cm−3 (identical to HKUST‐1 and below UTSA‐76) and 216 cm3 (STP) cm−3 (8 % greater than HKUST‐1 and 3 % greater than UTSA‐76) under a pressure swing of 65–5 bar and 80–5 bar, respectively, at 298 K. It should be noted that this performance is much higher than the Co analog: DUT‐23‐Co. [37]

Among all the MOFs examined, TV uptake is still the highest in the case of HKUST‐1 in both the high‐ and low‐pressure region. The increase in the UV capacities of UTSA‐76, UMCM‐152 and DUT‐23‐Cu relative to HKUST‐1 is attributed to their comparatively low methane uptake at 5 bar (DUT‐23‐Cu: 21 cm3 (STP) cm−3<UMCM‐152: 40 cm3 (STP) cm−3<UTSA‐76: 56 cm3 (STP) cm−3<HKUST‐1: 72 cm3 (STP) cm−3). From this trend it is apparent that the success of DUT‐23‐Cu is ascribed to less adsorbed CH4 at low pressure due to a lack of electrostatic interactions between CH4 molecules and CUS (CUS are absent in DUT‐23‐Cu), rather high uptake at high pressure. This is an important design concern, and its manifestation is more subtle than the phenomenon in low temperature hydrogen sorbents where the presence of CUS can degrade deliverable capacity dramatically. [28] Further, the uptake at 80 bar follows the order (DUT‐23‐Cu: 237 cm3 (STP) cm−3<UMCM‐152: 266 cm3 (STP) cm−3≈UTSA‐76: 266 cm3 (STP) cm−3<HKUST‐1: 272 cm3 (STP) cm−3). Thus, larger pore volume in DUT‐23‐Cu contributes to having relatively lower volumetric uptakes both at 5 bar (21 cm3 (STP) cm−3) and 80 bar (237 cm3 (STP) cm−3) respectively. The trend can be understood in the context of previous studies on IRMOF‐8‐RT, another MOF with large pores, where only 50–65 % of the pores are filled by adsorbed methane even at 89.4 bar. [47] Reduction of pore size with additional linker substituents resulted in higher volumetric uptake in the derivatives of IRMOF‐8‐RT. [48]

Although deliverable volumetric capacity is the primary figure of merit for an ANG system, gravimetric capacity also influences vehicular performance because it impacts the mass of the ANG system. Earlier studies have demonstrated that gravimetric capacity depends on the pore volume and BET surface area of MOFs.[ 9 , 49 ] For example, MOF‐200, [50] MOF‐210 [50] and Al‐soc‐MOF‐1 [51] with high BET surface areas of 4530, 6240 and 5585 m2 g−1 respectively, have high gravimetric uptakes but all suffer from low volumetric uptakes. On the other hand, HKUST‐1 possesses high volumetric methane uptake at the expense of poor gravimetric capacity. A strategy to design MOFs with high UV capacity without compromising gravimetric methane uptake requires balancing surface area and porosity. [52] In the present study, UTSA‐76, UMCM‐152 and DUT‐23‐Cu all outperform HKUST‐1 in terms of their respective total gravimetric (TG) uptakes for pressures exceeding ≈30 bar. In fact, the TG uptake both at 65 and 80 bar follows the same order as the MOF's respective surface areas: HKUST‐1: 1836 m2 g−1<UTSA‐76: 2700 m2 g−1<UMCM‐152: 3430 m2 g−1<DUT‐23‐Cu: 5300 m2 g−1. However, at 5 bar, the gravimetric uptake follows a similar trend as of volumetric capacity, Figure 3. The usable gravimetric (UG) capacities of all three MOFs exceeds HKUST‐1 under both pressure swing conditions, Table 1.

Figure 3.

Figure 3

High pressure CH4 isotherms. Measured total a) volumetric and b) gravimetric plots for UTSA‐76, UMCM‐152 and DUT‐23‐Cu. For comparison, the isotherm of HKUST‐1[ 13 , 16 ] is also shown.

In summary, the present study has identified promising MOFs for methane sorption computationally. Based on these predictions, three MOFs, UTSA‐76, UMCM‐152 and DUT‐23‐Cu, were synthesized and their measured capacities were observed to surpass the usable capacity of HKUST‐1, the benchmark for methane storage, under pressure swing conditions (Figure 4). Specifically, UMCM‐152 is demonstrated to outperform the volumetric deliverable capacities of all of the best MOFs, known so far, thus highlighting its promise in methane storage (Table S6). Although high uptake at elevated pressure is critical for achieving this performance, there is an additional requirement that the density of high affinity sites (coordinatively unsaturated metal centers) is low enough to allow relatively complete release of stored gas at low pressure. The utility of mining existing MOF databases for promising materials is demonstrated and provides an efficient discovery paradigm for measurements, such as high pressure methane storage, that are challenging experimentally.

Figure 4.

Figure 4

Comparison of measured usable capacities of top performing MOFs, HKUST‐1,[ 13 , 16 ] UTSA‐76, DUT‐23‐Cu and UMCM‐152 on a a) volumetric and b) gravimetric basis. Capacities are reported under a pressure swing of 80–5 bar at 298 K.

Conflict of interest

The authors declare no conflict of interest.

Supporting information

As a service to our authors and readers, this journal provides supporting information supplied by the authors. Such materials are peer reviewed and may be re‐organized for online delivery, but are not copy‐edited or typeset. Technical support issues arising from supporting information (other than missing files) should be addressed to the authors.

Supporting Information

Acknowledgements

Financial support for this study was provided by the US Department of Energy, Office of Energy Efficiency and Renewable Energy, Grant no. DE‐EE0008814.

K. Nath, A. Ahmed, D. J. Siegel, A. J. Matzger, Angew. Chem. Int. Ed. 2022, 61, e202203575; Angew. Chem. 2022, 134, e202203575.

Contributor Information

Prof. Dr. Donald J. Siegel, Email: Donald.Siegel@austin.utexas.edu.

Prof. Dr. Adam J. Matzger, Email: matzger@umich.edu.

Data Availability Statement

The data that support the findings of this study are available on request from the corresponding author. The data are not publicly available due to privacy or ethical restrictions.

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Data Availability Statement

The data that support the findings of this study are available on request from the corresponding author. The data are not publicly available due to privacy or ethical restrictions.


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