Mark D.
Allendorf
*a,
Zeric
Hulvey
*bc,
Thomas
Gennett
de,
Alauddin
Ahmed
f,
Tom
Autrey
g,
Jeffrey
Camp
h,
Eun
Seon Cho
p,
Hiroyasu
Furukawa
ij,
Maciej
Haranczyk
h,
Martin
Head-Gordon
ik,
Sohee
Jeong
jo,
Abhi
Karkamkar
g,
Di-Jia
Liu
l,
Jeffrey R.
Long
ijm,
Katie R.
Meihaus
i,
Iffat H.
Nayyar
g,
Roman
Nazarov
n,
Donald J.
Siegel
f,
Vitalie
Stavila
a,
Jeffrey J.
Urban
o,
Srimukh Prasad
Veccham
i and
Brandon C.
Wood
n
aEnergy & Transport Technology Center, Sandia National Laboratories, Livermore, CA 94551, USA. E-mail: mdallen@sandia.gov
bFuel Cell Technologies Office, U.S. Department of Energy Office of Energy Efficiency and Renewable Energy, Washington, DC 20585, USA. E-mail: Zeric.Hulvey@hq.doe.gov
cOak Ridge Institute for Science and Education, Washington, DC 20585, USA
dDepartment of Chemistry, Colorado School of Mines, Golden, CO 80401, USA
eNational Renewable Energy Laboratory, Golden, CO 80401, USA
fMechanical Engineering Department, University of Michigan, Ann Arbor, Michigan 48109, USA
gPacific Northwest National Laboratory, Richland, WA 99354, USA
hComputational Research Division, Lawrence Berkeley National Laboratory, Berkeley, CA 94720, USA
iDepartment of Chemistry, University of California, Berkeley, CA 94720, USA
jMaterials Sciences Division, Lawrence Berkeley National Laboratory, Berkeley, CA 94720, USA
kChemical Sciences Division, Lawrence Berkeley National Laboratory, Berkeley, CA 94720, USA
lChemical Sciences and Engineering Division, Argonne National Laboratory, Lemont, IL 60439, USA
mDepartment of Chemical and Biomolecular Engineering, University of California, Berkeley, CA 94720, USA
nLawrence Livermore National Laboratory, Livermore, CA 94550, USA
oMolecular Foundry, Lawrence Berkeley National Laboratory, Berkeley, CA 94720, USA
pDepartment of Chemical and Biomolecular Engineering, Korea Advanced Institute of Science and Technology (KAIST), Korea
First published on 13th August 2018
Nanoporous adsorbents are a diverse category of solid-state materials that hold considerable promise for vehicular hydrogen storage. Although impressive storage capacities have been demonstrated for several materials, particularly at cryogenic temperatures, materials meeting all of the targets established by the U.S. Department of Energy have yet to be identified. In this Perspective, we provide an overview of the major known and proposed strategies for hydrogen adsorbents, with the aim of guiding ongoing research as well as future new storage concepts. The discussion of each strategy includes current relevant literature, strengths and weaknesses, and outstanding challenges that preclude implementation. We consider in particular metal–organic frameworks (MOFs), including surface area/volume tailoring, open metal sites, and the binding of multiple H2 molecules to a single metal site. Two related classes of porous framework materials, covalent organic frameworks (COFs) and porous aromatic frameworks (PAFs), are also discussed, as are graphene and graphene oxide and doped porous carbons. We additionally introduce criteria for evaluating the merits of a particular materials design strategy. Computation has become an important tool in the discovery of new storage materials, and a brief introduction to the benefits and limitations of computational predictions of H2 physisorption is therefore presented. Finally, considerations for the synthesis and characterization of hydrogen storage adsorbents are discussed.
Broader contextThe widespread use of hydrogen as a clean, sustainable energy carrier has the potential to provide several significant benefits, including a reduction in oil dependency and emissions, improved energy security and grid resiliency, and substantial economic opportunities across many sectors. Hydrogen-fueled vehicles are already appearing internationally, and one of the critical enabling technologies for increasing their availability is on-board hydrogen storage. Stakeholders in developing a hydrogen infrastructure (e.g., state governments, automotive manufacturers, station providers, and industrial gas suppliers) are currently focused on high-pressure storage of H2 at 350 and 700 bar, in part because no viable hydrogen storage material has emerged. Novel adsorbents are an important category of storage materials that have attracted considerable interest because of their potential to meet all DOE targets and deliver hydrogen at lower pressures and higher on-board densities. Nevertheless, the most promising materials synthesized to date require cryogenic temperatures to maximize their capacity, and storage under such conditions is undesirable because it adds complexity and cost to the fuel delivery system. Consequently, a successful solid-state materials solution would significantly reduce costs and ensure the economic viability of a U.S. hydrogen infrastructure. |
The search for solid-state H2 storage materials that can supplant compressed gas systems has been ongoing for at least two decades. The development of a viable storage material would enable increased system-level capacities, thereby resulting in a reduction of the mass, volume, and cost requirements of the storage system. Furthermore, materials-based storage would enable lower operating pressures and potentially reduce other requirements such as pre-cooling at the fueling station, providing additional cost and energy savings to the driver. Among the various types of storage materials, porous adsorbents have the potential to offer rapid filling times and delivery response, long cycle life, and easily-controlled delivery pressures. However, several challenges remain in the development and implementation of such materials: both volumetric and gravimetric capacities for the best performing adsorbents are still well below the DOE targets (Table 1) and usable, system-level capacities can be significantly less than total uptake for a given material. Furthermore, it is difficult to extrapolate system-level performance from the typical laboratory measurements carried out to investigate adsorption properties for a given material. Several material design strategies have been proposed to address these challenges, and in 2010 the DOE-funded Hydrogen Sorption Center of Excellence (HSCoE) produced a report with recommendations for continuing material development efforts (see discussion below).4 Since then, the science of hydrogen storage has advanced considerably and some of these earlier recommendations are no longer valid while others have been amplified by subsequent discoveries. Moreover, new strategies have been proposed in recent years, some of which have received only cursory attention.
The objective of this Perspective is to evaluate the various current known and proposed strategies for improving the performance of hydrogen adsorbents, with an eye toward guiding current and ongoing research, as well as proposals to develop new storage concepts. This work also includes essential updates to the conclusions of the 2010 HSCoE report. In our analysis, the primary focus is on optimizing properties that currently represent major impediments to successful materials implementation, namely low isosteric heats of adsorption (Qst) and sub-par usable volumetric and gravimetric capacities. Clearly, there are other material properties that could significantly impact performance, such as material stability, durability, cyclability, adsorption kinetics, packing density, and system engineering effects; however, to include all of these criteria here is impractical. Consequently, we provide a short discussion of the most pertinent practical metrics for evaluating material utility and the various caveats associated with their optimization.
Theory and modeling are now valuable tools for guiding the design of new materials and for characterizing their performance, and hydrogen adsorbents are no exception. Advances in theory and computing power have greatly improved upon earlier models and in some cases have revised the conclusions of previous results. We deemed it important to also provide an abbreviated overview of theoretical methods and predictions and how they compare with current experiment-based understanding. Recommended methods and levels of theory considered to be the best for modeling specific aspects of adsorbent behavior are discussed. In particular, we address the demanding problem of accurately modeling the interaction energy of H2 with strongly binding sites in metal–organic frameworks (MOFs) and the accuracy of force fields used in atomistic modeling to predict H2 adsorption isotherms.
Finally, we provide guidance concerning the feasibility of synthesizing novel adsorbents, and the potential drawbacks associated with characterization tools used to evaluate them. As in the sections on theory and materials properties, this synthesis section is a concise summary rather than a comprehensive review. Our intention is ultimately to raise awareness of potential key issues so that they can be avoided in future research efforts and when reporting results.
Storage temperature is another complicating factor, and Fig. 1 also illustrates how the usable capacity of H2 in a given material can change with operating temperature (red and blue curves). As the DOE targets only address hydrogen delivery temperature (−40 to 85 °C, to meet fuel cell system operation specifications) and not the storage system operating temperature, a range of possible system designs can be considered. Materials-based systems designed to operate at lower temperatures may require more complex and costly BOP components (e.g., thermal insulation, heat exchangers) and will therefore likely impart more penalties on the system-level capacity compared to systems designed to operate at ambient temperatures.8 Adsorbent systems could also incorporate a temperature swing step, for example from 77 to 160 K, which increases usable capacities by increasing the quantity of H2 desorbed upon cycling. Systems operating at lower temperatures will also likely require materials with significantly higher capacities compared to ambient temperature systems to compensate for insulation and additional system complexity; unfortunately, there is no simple factor that can be applied to quantify this requirement. Tank design aspects constitute more of an engineering challenge than a materials challenge, and we will not address them in detail here. While it is important to keep operating temperature in mind when comparing the behavior of different adsorbents, it is not necessary to discount a specific class of materials specifically because of operating temperature—the focus herein is on material strategies to increase capacities for any adsorbent.
Historically, much of the early focus on materials development was toward maximizing adsorbent surface area to achieve the necessary gravimetric capacities, and the discovery of ultrahigh surface area materials such as the MOF NU-100 (reported Brunauer–Emmett–Teller [BET] surface area of 6143 m2 g−1) generated excitement that the DOE targets could soon be met.9 This optimism was supported by empirical observations that maximum excess gravimetric capacity increased approximately linearly with increasing surface area, at the rate of ∼1 wt% per 500 m2 g−1 for adsorption at 77 K and moderate pressures of ∼35 bar, commonly referred to as Chahine's rule.10,11 There are some exceptions to this rule, for example in selected carbons an increase in pore size can result in a net decrease in gravimetric H2 uptake, even though the surface area increases.12 Adsorbents that demonstrate very strong binding of H2 can also exhibit gravimetric capacities that exceed those predicted by this relationship.
As more high surface area materials were synthesized, it became apparent that exceptional gravimetric capacity often comes at the expense of volumetric capacity. This relationship was reported by Siegel and coworkers, who analyzed the trend between total volumetric and gravimetric capacity calculated for ∼4000 porous materials extracted from the Cambridge Structural Database (Fig. 2). Notably, the authors found that total volumetric capacity is at a maximum for materials with surface areas ranging from 3100–4800 m2 g−1.13 It is unclear whether the trade-off between gravimetric and volumetric capacities represents a peculiarity specific to materials that have been synthesized to date, or instead reflects a universal feature of H2 uptake in adsorbents. Subsequent reports have highlighted the effect of hydrogen storage densities on driving range; these analyses argue that FCEV driving range is more strongly tied to volumetric capacity than gravimetric capacity.6,14,15 Adsorbents with exceptional gravimetric capacities may therefore not be very attractive from a systems-level standpoint, and it is essential that both gravimetric and volumetric capacity be considered simultaneously when analyzing the viability of a specific adsorbent.
Fig. 3 takes these analyses a step further by illustrating the dependence of H2 uptake on adsorbent structural features; here, the simulated total volumetric and gravimetric capacities of a database of MOFs13,14,16 are plotted with respect to five crystallographic properties: density, pore volume, pore diameter (defined as the largest diameter of any internal cavity), gravimetric surface area, and volumetric surface area. The total capacities approximate the usable capacities that could be achieved using a combined temperature–pressure swing process, from T = 77 K and P = 100 bar to T = 160 K and P = 5 bar. Thus, as mentioned above, these total capacities correspond to an upper limit for the amount of H2 that could be delivered by the given material storage system. The ranges of these crystallographic properties that optimize gravimetric and volumetric performance are summarized in Table 2.
Fig. 3 Total gravimetric (top) and volumetric (bottom) capacities as a function of various crystallographic properties for 5309 MOFs extracted from the UM and CoRE databases.13,16 Capacities were calculated at 77 K and 100 bar using Grand Canonical Monte Carlo (GCMC) simulations with the pseudo-Feynman–Hibbs interatomic potential.17–19 |
Crystallographic metric | Range |
---|---|
Density (g cm−3) | 0.4–0.5 |
Pore volume (cm3 g−1) | 1–2 |
Pore diameter (Å) | 10–20 |
Gravimetric surface area (m2 g−1) | 4500–5500 |
Volumetric surface area (m2 cm−3) | 1500–2250 |
Turning first to the dependence of total capacity on MOF density, Fig. 3a shows that gravimetric capacity monotonically decreases with increasing density. In contrast, total volumetric capacity (Fig. 3b) first increases as density increases from zero to ∼0.5 g cm−3, but then drops off for higher densities. These data suggest that maximizing gravimetric and volumetric performance simultaneously can be achieved with densities between 0.4 and 0.5 g cm−3.
With both increasing pore volume and diameter, the gravimetric capacity increases monotonically (Fig. 3c and e, respectively), although the trend is more pronounced in the case of pore volume (Fig. 3c), as might be expected given Chahine's rule (albeit at a higher pressure of 100 bar). The total volumetric capacity displays a non-monotonic dependence on both pore volume and diameter (Fig. 3d and f, respectively), initially increasing with increasing volume and diameter to reach a maximum value for volumes between 1 and 2 cm3 g−1 and diameters between 10 and 20 Å, before decreasing for larger values.
The influence of gravimetric and volumetric surface area on H2 capacity is illustrated in Fig. 3g–j. As expected from Chahine's rule, gravimetric capacity correlates roughly linearly with gravimetric surface area (Fig. 3g). In contrast, the relationship between total volumetric capacity and gravimetric surface area (Fig. 3h) is reminiscent of that observed in Fig. 2: MOFs with very high surface areas (coinciding with large gravimetric capacities) tend to exhibit poor volumetric performance.13 From this data, it is clear that MOFs with gravimetric surface areas ranging from 4500 to 5500 m2 g−1 present a reasonable compromise in balancing gravimetric and volumetric performance. Unsurprisingly, volumetric capacity increases with volumetric surface area in a linear fashion (Fig. 3j), with the highest capacities exhibited by MOFs with surface areas >2000 m2 cm−3. The relationship between gravimetric capacity and volumetric surface area is more complex: although the capacity of most MOFs increases linearly with increasing surface area, the highest capacities are exhibited by several materials with volumetric surface areas in the range of 1000–2000 m2 g−1. Thus, volumetric surface areas between 1500 and 2250 m2 g−1 serve to maximize both gravimetric and volumetric performance.
Additional studies have examined this interplay between gravimetric and volumetric capacities and suggested ranges similar to those given in Table 2 for structural properties that optimize adsorptive H2 storage at cryogenic conditions.20–23 For example, Thornton and coworkers trained a neural network to predict hydrogen uptake across a diverse collection of adsorbents, including MOFs, covalent organic frameworks (COFs), zeolites, zeolitic imidizolate frameworks (ZIFs), and porous polymer networks.20,24 Their model identified several MOFs as amongst the highest capacity materials, with predicted optimal ranges for pore diameter and surface area that closely match those from the MOF-only dataset represented by Fig. 3 and Table 2. This result suggests that these ranges may serve as a reasonable approximation for target structural features in other non-MOF classes of adsorbents, at least under cryogenic conditions.
Can additional optimization of the intrinsic framework structural features increase capacity even more? Metal–organic frameworks already excel on a gravimetric basis, as seen in Fig. 3, with some compounds predicted to exhibit capacities exceeding 15 wt%. On the other hand, under the cryogenic conditions utilized in this study, no known MOFs exhibit total volumetric capacities exceeding 60 g L−1. Given that some MOFs exhibit adsorbed H2 densities comparable to that of liquid or solid H2 (70–76 g L−1), a lofty goal would be to achieve these densities on a total capacity basis, i.e., factoring in both adsorbed and gas-phase H2. Thus, developing new MOFs that improve volumetric performance, without sacrificing high gravimetric density, presents one path forward.
At temperatures and pressures above its boiling point, the first monolayer of H2 adsorbed at a solid surface typically exhibits adsorption enthalpies in the range of ∼1–10 kJ mol−1.26 While adsorption enthalpies are reported on a rather limited basis due to measurement challenges, available literature data indicate that enthalpies larger than 10 kJ mol−1 are relatively rare and are mainly found in doped carbons,27 functionalized zeolites,28 and MOFs29 with structural features that impart strong metal–hydrogen interactions (Fig. 4). Examples of some of these materials will be described in detail later in this Perspective. The available literature adsorption enthalpies can be investigated as a function of gravimetric capacity as shown in Fig. 4, and this data reveals that maximum gravimetric uptake at cryogenic temperatures tends to correlate with H2 adsorption enthalpies near 5 kJ mol−1.26,30–33 Qualitatively, a similar trend is observed for volumetric capacities as a function of adsorption enthalpy, although this comparison is difficult as volumetric capacities can be determined in different ways (e.g., utilizing the bulk vs. packing density of a material), resulting in substantially different values.
Fig. 4 Excess gravimetric H2 uptake versus enthalpy of H2 adsorption for various classes of hydrogen storage materials. The adsorption enthalpy values were taken from ref. 26 and 30–33 and are reported at cryogenic conditions, typically between 77 and 87 K. |
A few studies have noted that adsorption enthalpies in the range of 15–25 kJ mol−1 H2—corresponding to H2-framework interactions intermediate between strong physisorption and weak chemisorption—are optimal targets for reversible hydrogen storage.25,34,35 It is important to highlight that these analyses assume a system operating at near-ambient conditions, and adsorption enthalpies are intimately tied to system storage temperatures. Generally speaking, materials with higher heats of adsorption are more likely to exhibit impressive room temperature hydrogen storage behavior. However, because these materials can exhibit steep capacity increases at low pressures, very high heats of adsorption can actually lower usable capacity at a given temperature due to a large amount of inaccessible H2 that remains adsorbed below 5 bar. As the isotherm slope increases, usable capacity will eventually begin to decrease, therefore requiring an upper limit on targeted heat of adsorption values. This balance between high heat of adsorption and optimal usable H2 capacity must be considered when comparing classes of storage materials.
Camp and Haranczyk recently investigated the impact of temperature and binding energy on adsorbent usable capacity, and the results of this study are reported here for the first time. The analysis focused on a model material with the same structure as M2(dobdc) (M-MOF-74 or CPO-27-M; M = Mg, Mn, Fe, Co, Ni, Cu, or Zn; dobdc4− = 2,5-dioxido-1,4-benzenedicarboxylate), which contains the highest density of open metal sites of any known framework. The adsorption energy of H2 in M2(dobdc) was modeled by mixing Lennard-Jones parameters for each atom in the structure with Lennard-Jones parameters for hydrogen atoms. For example, the adsorption energy between a framework Mg2+ site and an adsorbed H2 molecule was calculated by using values of σH2 = 2.958 Å and εH2 = 36.7 K36 and σMg = 2.961 Å and εMg = 55.895 K37 in the Lorentz–Berthelot mixing rule38 and applying the 12-6 Lennard-Jones equation:
(1) |
In this model system, the H2-open metal site interaction energy was artificially altered by varying the ε parameter for each metal from 0 to 2 × 104 K, yielding interaction energies of 0–163 kJ mol−1. This variation allowed for the simulation of hypothetical binding interactions with H2 heats of adsorption (at low coverage) as high as 16 kJ mol−1. As a means of probing the effect of strong binding site density, an additional variable corresponding to the fraction of active open metal sites was introduced. This approach was realized by assigning a portion of the total metal sites a dummy value of ε = 0 K, effectively making them inactive for H2 binding. Each pixel on the heat map plots in Fig. 5 corresponds to the output of an independent Grand Canonical Monte Carlo (GCMC) simulation at a given active open metal site concentration (x-axis) and open metal site interaction strength (y-axis).
These simulations showed that at cryogenic temperatures (77 K, Fig. 5b), open metal sites with high interaction energies are not needed to maximize H2 usable capacity, because the enhancement these sites provide results in a large percentage of the adsorbed H2 binding at very low pressures. Thus, a considerable portion of the H2 remains bound to the material in the discharged state at 5 bar and therefore cannot be utilized as fuel. At near-ambient temperatures (243 K, Fig. 5d), stronger and more open metal sites are desired to increase usable capacity, because isotherms are much flatter in the low-pressure region and less H2 is bound to the material in the discharged state. At intermediate temperatures (180 K, Fig. 5c), there is an interesting interplay between these effects—materials that have fewer open metal sites display fairly constant usable capacities regardless of the binding strength at those sites, and materials with more open metal sites display higher usable capacities as the binding strength at those sites decreases.
This work demonstrates that estimating system-level performance is more complicated than simply targeting materials with binding strengths within a specific range, highlighting that the proposed 15–25 kJ mol−1 target enthalpy range for adsorbent materials is only applicable to a certain set of storage conditions at ambient temperatures. We note that this study was carried out for gravimetric capacity only and that as a similar study on volumetric capacity would be valuable. An ideal study would combine, in some form, the two types of sensitivity analyses described in this section, investigating the effect of optimizing both pore structure and strong binding sites. We expect that further development of high throughput simulation approaches and material databases (including both real and hypothetical structures) will enable such analyses. Machine learning techniques will likely play a role in simplifying resulting data into practical materials design rules.
Finally, we note that the entropy change upon H2 adsorption can also influence the overall adsorption thermodynamics, and the magnitude of this value is dominated by the loss of the hydrogen gas entropy in the form of translational, vibrational, and rotational degrees of freedom.35,39,40 However, it is believed that ΔH has a greater effect on the overall thermodynamics of hydrogen adsorption in adsorbents. As a general rule, increasing the strength of the interaction between the H2 molecule and the storage material—except for a few special cases and conditions, such as when this increase results in decreased deliverable capacities—appears to enhance overall material performance, and a major thrust of current materials development efforts are focused on strategies to optimize this interaction.
Method | Key properties determined | Typical accessible scales | Benefits | Limitations and challenges | Sample references | |
---|---|---|---|---|---|---|
Static first principles | Ab initio wavefunction methods (quantum chemistry) | Binding energies, vibrational frequencies within static approximation | 50–100 atoms, depending on method | High accuracy (especially CCSD(T)), including explicit evaluation of correlation | Very high computational expense; limited to finite cluster models; no dynamical information; limited scalability on modern architectures | 41–43 and 59–61 |
Quantum Monte Carlo (QMC) | Binding energies | ∼100 atoms | High accuracy, including explicit evaluation of correlation; provides systematic statistical measure of convergence; can be applied to clusters or extended systems; highly scalable on modern architectures | Very high computational expense; no dynamical information, explicit forces, or structural optimization; requires geometry inputs from DFT or experiments | 44–46 and 62–67 | |
Static density functional theory (DFT) with van der Waals corrections | Binding energies, vibrational frequencies within static approximation | ∼1000 atoms | Generally offers best overall tradeoff between accuracy and computational expense; can be applied to clusters or extended systems | Intermediate computational expense; accuracy is dependent on choice of XC functional, which is not always straightforward | 47–50 and 68–70 | |
Dynamical | Ab initio molecular dynamics (AIMD) | Dynamic vibrational frequencies; entropy; enthalpy contributions from gas–gas interactions | Hundreds of atoms (<100 ps) | Based on DFT, so it accounts for polarization, hybridization, charge transfer, etc. within dynamics; explicitly captures anharmonic contributions to entropy; can include relaxation of sorbent geometry | Intermediate to high computational expense; short time scales complicate convergence of statistical quantities; difficult to simulate large frameworks or amorphous systems; no quantum nuclear effects; usually requires fixing total H2 molecules; inherits same limitations as DFT | 51–53 |
Classical molecular dynamics and empirical force-field methods | Adsorption enthalpy; entropy; enthalpy contributions from gas–gas interactions | Millions of atoms (depends on complexity of force field; ∼1 ns) | Can access much longer scales than first-principles methods; low computational expense for robust convergence of thermodynamic quantities; can include quantum nuclear effects approximately; can include relaxation of sorbent geometry (with properly parameterized potentials) | Parameterization and accuracy validation are difficult; poor transferability; can fail to capture physics of stronger-binding interactions and anharmonicity; usually requires fixing total H2 molecules | 57 and 71–74 | |
Statistical mechanical | Grand Canonical Monte Carlo (GCMC) | Full pressure–temperature–composition equilibria; adsorption isotherms | Determined by method for energy computation (usually similar to classical MD) | Robust statistical–mechanical method allows for calculation of composition-dependent equilibria; allows for variation of total H2 molecules; typically uses empirical force fields for accessing long scales | Accuracy and limitations depend on method for computing interaction energy (usually empirical force fields); no dynamical information; vibrational/rotational/translational entropy must be computed separately; most implementations assume fixed sorbent geometry | 56–58, 75 and 76 |
The second category consists of dynamical methods, which have the advantage of providing explicit properties at finite temperatures, including enthalpy contributions from gas–gas interactions, as well as vibrational, rotational, and translational entropy contributions. This treatment provides specific advantages for accurately computing the entropy of systems with intermediate-strength binding, for which the available degrees of freedom cannot otherwise be readily approximated. Approaches include ab initio molecular dynamics based on DFT51–53 and classical molecular dynamics based on empirical force fields.54
The third category of computational approaches includes statistical–mechanical methods for computing equilibrium thermodynamics—most notably, GCMC simulations.54–58 These simulations use a stochastic Monte Carlo approach that varies the number of H2 molecules as well as their positions. This strategy permits evaluation of thermodynamic equilibrium properties at any constant H2 pressure. The advantages of GCMC make it the most widely used technique for evaluating full H2 adsorption isotherms, the results of which can be directly compared with experimental data. Because GCMC simulations generate many individual configurations, the corresponding energies are usually evaluated with empirical force fields for computational efficiency.
In the following sections, we explore some of the challenges in accurately predicting H2 physisorption using several of the abovementioned techniques, including key sources of error. We also provide an overview of current trends in the development of improved methods and offer recommendations for best practices, including acceptable concessions when choosing between computational efficiency and accuracy.
Rank | Functional | RMS error (kJ mol−1) |
---|---|---|
1 | ωB97M-V | 0.75 |
2 | B97M-rV | 0.91 |
3 | ωB97X-V | 0.99 |
4 | B97M-V | 0.99 |
5 | B3LYP-D3(CSO) | 1.27 |
13 | BLYP-D3(BJ) | 1.42 |
25 | TPSS-D3(CSO) | 1.53 |
62 | PBE-D3(CSO) | 1.89 |
115 | PBE-D2 | 2.69 |
159 | PBE | 8.19 |
Nevertheless, although improving quantitative accuracy remains the goal of DFT XC functional development, it is worth emphasizing that qualitative trends in binding energy are often reproduced even with comparatively simple functionals, including generalized gradient approximations (GGAs) with standard −D corrections. Indeed, most modern dispersion-corrected DFT methods (such as those in Table 4) tend to give consistent trends for binding that are derived almost exclusively from dispersion forces. For adsorbent materials that feature significant H2 interactions beyond dispersion, as is generally the case for the most promising hydrogen storage materials, the results can be more varied. While permanent electrostatic effects are typically adequately described even by the simplest DFT XC functionals, treatment of more complex contributions such as Lewis acid–base interactions and backbonding, which involve charge transfer, induction, and orbital hybridization,59,60 can differ broadly across functionals (see Fig. 6 for an example). In these latter cases, predicted trends should be treated with a degree of caution unless the most sophisticated XC functionals are employed, since individual physical contributions may be treated at different levels of accuracy. As a general rule, the safest approach when evaluating the reliability of a predicted binding trend is to limit comparisons to systems for which the primary underlying physical interaction is very similar. This allows one to take advantage of intrinsic error cancellation. Notably, there have also been recent efforts to introduce error estimation directly into the formulation of the XC functional.85
Fig. 6 Hydrogen physisorption energies (colored data points) at different binding sites in Cu2(bptc) (MOF-505) predicted using lower-level GGA DFT functionals (PBE, BLYP) and several different formulations of van der Waals-corrected and meta-GGA DFT functionals (Dion, optB88, optBPE, optB86b, TPSS, TS, PBE+D2, PBE+D3).68,79,88–91 Results are compared with the one-σ (68%) confidence interval obtained from QMC runs (grey shaded region). Geometries for each of the sites (bottom) were fixed to those obtained from PBE+D3 and exhibit little variation with the chosen method, unlike the binding energies. The systematic statistical nature of QMC allows for downselecting appropriate DFT functionals for different types of binding sites, with confidence levels based on the degree of QMC convergence. |
Quantum Monte Carlo (QMC) is an alternative benchmark method for modeling noncovalent interactions that affords similar accuracy to CCSD(T) and yet can be applied equally to molecular clusters or to extended periodic systems.44–46 To date, most QMC calculations of H2 physisorption have focused on molecular clusters, including Ca2+ complexes,62,63 certain metal–organic complexes,64,67 and aromatic carbon complexes.65,66 The results of these calculations can vary significantly from DFT with simple XC functionals; for instance, in the case of Ca2+, QMC predicted that the binding of four H2 molecules is energetically unstable or hardly stable (and then only at 0 K),62,63 in contrast with earlier DFT and MP2 calculations that predicted stable binding of up to eight H2 molecules.86,87 Likewise, Fig. 6 shows substantial discrepancies between QMC binding energies of H2 on Cu2(bptc) (MOF-505; bptc4− = 3,3′,5,5′-biphenyltetracarboxylate) and a number of DFT-based results; such analyses can aid selection of the best DFT XC functionals. An important qualification for QMC is that input geometries must be precisely known (e.g., from neutron diffraction) or obtained using DFT or another lower level of theory.
These shortcomings suggest the use of a hybrid approach, in which first-principles-derived binding energies are used to parameterize force fields for the stronger-binding interaction sites (often aided by energy decomposition analysis to isolate individual physical contributions95–97), with reliance on more standard force-field formulations for H2 intermolecular interactions and weaker-binding sites. The development and assessment of system-specific force fields for H2 binding and release in adsorbents is a topic for a review in itself.58,98–100 Note that most of the articles referenced here are not specific to H2, but the successful approaches are generic to the binding of any small, non-polar, closed-shell molecule in a nanoporous framework.
Alternatively, entropic contributions can be computed directly from finite-temperature molecular dynamics (either ab initio or classical methods). One promising approach for using dynamics trajectories to interpolate and extrapolate entropy over a broad range of temperatures is the two-phase thermodynamic method of Lin et al.106 This method has been used to evaluate the entropy of pure CO2, as well as adsorbates confined within zeolites, suggesting a similar approach may be adopted to obtain accurate entropies of bound H2.107,108
The most widely used approach for incorporating nuclear quantum effects is to modify GCMC and classical molecular dynamics via a so-called Feynman–Hibbs potential.113 Reasonably good agreement with experimental results has been obtained for H2 adsorption in a range of MOF systems using this approach.14 Another recent example is H2 adsorption in Zr6O4(OH)4(bdc)6 and Zr6O4(OH)4(bpdc)6 (known as UiO-66 and UiO-67, respectively; bdc2− = 1,4-benzenedicarboxylate, bpdc2− = biphenyl-4,4′-dicarboxylate).75 Full path-integral formulations of GCMC have also been recently explored.76
The main alternative to cluster models is the use of periodic boundary conditions (PBCs), which is a natural approach in conjunction with periodic plane-wave basis functions that are commonly used for solid-state DFT calculations.115 However, these models can be more limited in their accuracy; for instance, while dispersion-corrected GGAs are widely used for PBC-DFT calculations, higher-accuracy functionals are less common due to their high computational cost. It is possible to employ cluster-based corrections to PBC-DFT calculations to achieve greater accuracy in modeling local interactions; examples of their application include H2 binding in MOF-5 (Zn4O(bdc)3) and recent work on CO and N2 binding in Mg-MOF-74.116,117
In practice, the presence of disorder and heterogeneity can make it impossible to derive an exact model for many adsorbents, particularly within the size constraints of simulation supercells that are accessible to first-principles methods. Instead, a broader picture of the interaction of a material with hydrogen must be derived from simpler representative fragment models. This strategy is best justified if the dominant physical interaction is relatively short-range; examples include interactions with specific functional groups or substitutional defects that introduce polarization and/or partial charge transfer.120 The actual material may incorporate many different types of functional groups or defects, which can be investigated within the fragment models. However, because this approach does not generate an integrated material model, one cannot utilize GCMC simulations to simulate isotherms over the full pressure range. An alternative is to generate a single representative model based on fragments, provided the computational expense of the larger model can be handled. This hybrid approach has been demonstrated by Singh et al., wherein carbon foam models were constructed by fusing carbon nanotube fragments.112 These integrated models were then varied systematically and used to examine H2 adsorption via GCMC simulations.
Adsorbents are not porous until solvent or other pore-templating molecules are removed from the as-synthesized material. This activation process is most simply carried out by heating the material under vacuum, but if this approach is not sufficient, or results in some amount of structural degradation, then more complex solvent exchange methods may be necessary.130 Materials that contain very large pores, high surface areas, or solvent molecules bound to metal sites in the framework are typically more challenging to activate. Following synthesis, some strongly metal-bound solvent molecules (e.g., N,N-dimethylformamide [DMF]) can be removed by first performing a solvent exchange, wherein the as-synthesized material is soaked in a lower-boiling or more weakly coordinating solvent (e.g., chloroform or methanol). Over the course of a few days—during which time the soaking solvent is replenished several times—the strongly-bound solvent is gradually displaced and washed from the framework in favor of the soaking solvent. The latter can then be removed from the material by mild heating under vacuum.29 Drying with supercritical CO2 drying has become a widespread approach over the last decade, as it has been demonstrated that the negligible surface tension of the carbon dioxide allows for the activation of more delicate structures that otherwise might collapse upon heating. This method is now used commonly by MOF researchers to achieve high surface areas.131–133
Regardless of the activation method used, it is of utmost importance to ensure that the extent of activation and chemical composition of the material is known. Activation protocols should be accompanied by combined thermogravimetric analysis and mass spectrometry (TGA-MS) experiments, and routine analysis such as IR spectroscopy can be used to identify stretches arising from solvent molecules, decomposition products, or other impurities. For crystalline materials, powder X-ray diffraction patterns collected before and after activation should be measured to confirm that minimal degradation has occurred. Surface area and pore volume measurements should also be carried out and compared to predictions from crystal structures when possible, to ensure optimum material porosity. Even in rare cases where complete activation of the material is not necessarily desired, a quantitative knowledge of the material composition is still essential to understand adsorption data or cycling ability. Following activation, materials should be handled under inert conditions, regardless of how air- or water-sensitive the samples are, in order to ensure the activated material remains pristine. We note that confirmation that an adsorbent is fully activated is becoming even more critical as synthetic complexity increases, for example for materials targeted to bind more than one H2 molecule at an individual open metal site.134 Activation processes for these materials may likely be considerably more difficult than those known to date, and side products or species remaining from metalation reactions or post-synthetic modification will need to be accounted for and completely removed.
Investigation of the adsorption properties of a given material should commence only once diligent activation and characterization procedures have been used to establish that a material is permanently stable, porous, and of known stoichiometry. There are many reviews and documents available to provide guidance on best practices pertaining to hydrogen isotherm collection and data analysis, and the potential errors and difficulties associated with these measurements.5,135,136 Although improper technique in the measurement of adsorption data can result in inaccurate data, even a properly measured isotherm can be corrupted by a sample that has not been properly activated or handled; unfortunately, in such cases the resulting data do not always appear incorrect or anomalous. Consequently, it is advisable that samples prepared for gas adsorption measurements undergo a degassing step prior to isotherm collection, ideally monitored by mass spectrometry. Desorption and cycling measurements are highly recommended, as these can provide both isotherm quality control and verification of reversibility. A desorption isotherm for a physisorptive material that does not exhibit a large degree of flexibility or a pore-opening mechanism should closely mirror the adsorption isotherm; if it does not, then either an instrumental error, sample degradation, or a side reaction with hydrogen may have occurred.137 Side reactions can occur in materials with residual reactive groups or surface oxides, resulting in the formation of water or other bound molecules and erroneously high adsorption capacities. However, simple characterization methods can be used post-isotherm collection to check for these reactions.
It is also important to consider sample size when carrying out capacity and other measurements. In general, larger sample size improves the accuracy of isotherm measurements for reasons that are described in detail in the previously referenced best practices document.135 Often novel adsorbents are prepared using synthetic procedures that yield only small sample sizes, but the suite of high-quality characterization methods described above will typically require gram-scale amounts of adsorbent material to produce the most reliable data. Although increasing material yields beyond a few grams is often secondary to initial exploratory synthesis efforts, it is important to keep in mind that a material that requires difficult or expensive preparation may have diminished utility as a viable storage material. A techno-economic analysis was recently published for three MOFs in the M2(dobdc) series (M = Ni, Mg, Zn) and provides some valuable insight concerning the aspects of synthetic procedures contributing most to material cost.138
Investigations into the nature of hydrogen adsorption beyond storage capacity require additional characterization tools; for example, variable-temperature capacity measurements are commonly used to calculate Qst. Temperature-programmed desorption measurements can also provide information regarding the magnitude of H2 binding at strong adsorption sites. In addition, in situ variable-temperature diffuse reflectance infrared spectroscopy measurements are used to determine the enthalpy of adsorption at a particular binding site.29,139 For crystalline adsorbents, neutron powder diffraction on deuterium-loaded samples is an extremely powerful technique to elucidate crystallographic binding sites for H2 molecules.29,134,140 This method has been extensively used to investigate H2 bound at open metal sites in MOFs and other strong binding sites, as well as to explain adsorption behavior and direct subsequent synthetic efforts. Inelastic and quasi-elastic neutron scattering techniques can provide further site-specific binding details and insights into H2 diffusion behavior.141,142 Finally, although here we are focused on materials challenges, is important to note that it is now possible to predict systems-level performance on the basis of material property data alone, using recently developed models that are continually being updated and are publicly available online for use by researchers.143
Since then, it has been confirmed theoretically and experimentally that the gravimetric storage limits of materials demonstrating the spillover mechanism are sufficiently low to prevent them from being viable for onboard storage.148 Investigators have also discovered that effects such as metal oxide reduction of catalyst particles and irreversible hydrogenation reactions plague many spillover materials.137,149 Many of the previous reports of high capacities in spillover materials ultimately could not be reproduced, leading to an extended debate in the literature concerning several of the assumptions that drove research on these materials around the time of the HSCoE report.121,150–156 Consequently, spillover materials are no longer a significant focus of hydrogen storage materials research.
As mentioned previously, detailed characterization of H2 adsorption at framework open metal sites can in some cases be afforded by techniques such as in situ neutron diffraction and diffuse reflectance infrared spectroscopy. In 2006, low temperature neutron diffraction studies of Mn-BTT revealed that H2 adsorption primarily occurs at the exposed Mn2+ sites of the square planar Mn4Cl units (Fig. 7).140 The distance between Mn and D2 determined from these measurements (2.27 Å) was much shorter than observed previously between D2 and the saturated Zn4O(CO2)6 cluster of MOF-5 (∼3.1 Å).162 Strong binding due to polarization of the H2 molecule was supported by a distinctive downshift of the adsorbed H2 stretching band (4038 cm−1) compared to that in MOF-5 (4128 cm−1), observed by in situ IR spectroscopy.114,163 The IR absorption band at 4038 cm−1 evolved gradually as the temperature was lowered from 150 to 14 K, with two peaks arising at 4126 and 4133 cm−1 (below 100 K) and a third absorption band appearing at 4140 cm−1 (below 40 K). Here, the band at 4038 cm−1 corresponds to the adsorption of H2 at the Mn2+ sites and, importantly, the temperature dependence of this peak can provide a means of determining the thermodynamic parameters for adsorption at these specific sites.29,114 From the van’t Hoff plot, the magnitude of the ΔH value for the primary binding sites in Mn-BTT was estimated to be −11.9 ± 0.6 kJ mol−1, which is slightly greater than the Qst for Mn-BTT (−10.1 kJ mol−1), extracted from low-pressure H2 adsorption measurements.114,140 Note that such differences are typical since the Qst values are averaged over all adsorbed H2 species.
Fig. 7 (top) Molecular structures of organic linkers and inorganic building units comprising the Mn-BTT, Co2(dobdc), and Co2(m-dobdc) MOFs. (bottom) Crystal structures of each framework loaded with D2 (16 molecules per Mn4Cl unit in Mn-BTT and 2.25 D2 per Co2+ for Co2(dobdc) and Co2(m-dobdc)). Gray, red, dark blue, blue, and purple spheres represent C, O, N, Mn, and Co atoms, respectively. Deuterium molecules adsorbed at primary, secondary, ternary, and quaternary sites are shown in large orange, light green, pink, and white spheres, respectively. D2-framework interactions for the primary binding site are drawn as dotted lines. Hydrogen atoms of organic linkers are omitted to clarify.29,140 |
Owing to their high concentration of coordinatively-unsaturated metal sites, the M2(dobdc) family of frameworks (M = Mg, Co, Ni, Mn, Fe, and Zn) have also been heavily explored for H2 storage (Fig. 7). In this structure type, M2+ ions are connected through 2,5-dioxido-1,4-benzene-dicarboxylate linkers to form one-dimensional hexagonal channels that extend along the c-axis of the crystal, and the octahedral coordination environment of each metal in the as-synthesized material is completed by a solvent molecule. This solvent is readily removed with heating under vacuum to yield one-dimensional channels replete with open metal sites. Hydrogen adsorption has been extensively investigated in this series29,164–166 and it has been shown that at low pressures the strength of the metal–H2 interaction is highly dependent on the identity of the framework metal ion. From H2 isotherm measurements, the Qst value for Ni2(dobdc) was estimated to be −11.9 kJ mol−1,29 and across the entire series the −Qst values follow the trend Zn2+ < Mn2+ < Fe2+ < Mg2+ < Co2+ < Ni2+. This trend in the metal–H2 interaction strength generally follows the Irving–Williams series for high spin octahedral transition metal complexes, such that the −Qst values increase as metal ion radius decreases.167
More recently, the structural isomer of M2(dobdc), M2(m-dobdc) (m-dobdc4− = 4,6-dioxido-1,3-benzenedicarboxylate, M = Mg, Mn, Fe, Co, Ni) (Fig. 7), was identified as a promising alternative material for H2 adsorption, due to the greater charge density of its open metal sites and the lower cost of the organic linker.29 Interestingly, although the porosity of the M2(m-dobdc) series is similar to that of M2(dobdc), the former materials exhibit higher H2 uptake at 77 K and 1 bar, associated with −Qst values that are larger by 0.4–1.5 kJ mol−1 when comparing metal congeners. For example, the Qst value for Ni2(m-dobdc) was estimated from low-pressure H2 isotherms to be as large as −12.3 kJ mol−1, compared to a slightly smaller magnitude of −11.9 kJ mol−1 for Ni2(dobdc). While the significance of this difference could be debatable in the absence of error, values of ΔH for the Ni–H2 interaction in Ni2(m-dobdc) and Ni2(dobdc) were estimated from in situ IR spectroscopy to be −13.7 and −12.3 kJ mol−1, respectively, supporting a much stronger H2 interaction in the former material. Rigorous comparison of M2(m-dobdc) and M2(dobdc) materials via neutron diffraction, IR spectroscopy, and electronic structure calculations revealed that a subtle difference in the local metal environment leads to an increased positive charge density at the open metal sites of the M2(m-dobdc) compounds, promoting greater charge transfer from H2 to the metal center and leading to an enhanced metal–H2 interaction energy.29 Neutron diffraction characterization of Ni2(m-dobdc) also revealed tight packing of adsorbed D2 and a short D2⋯D2 contact of 2.82 Å between molecules adsorbed at primary and secondary sites (Fig. 7). This distance is even smaller than the distance of 3.23 Å observed between molecules in solid H2 at 5 K and highlights the potential for strong primary binding sites to promote a significant increase in the density of adsorbed H2 within the entire pore structure.168 These favorable H2–Ni2+ interactions and resulting efficient confinement of H2/D2 within the pores of Ni2(m-dobdc) result in this framework exhibiting the highest storage capacity to date for an adsorbent operating at 298 K and pressures up to 100 bar. Notably, when used in a process with temperature swings between −75 and 25 °C, this material achieves a usable volumetric capacity of 23.0 g L−1 in the pressure range of 5–100 bar.169
Metal cation exchange reactions have also been explored with MOFs as a means of tuning their gas adsorption properties, including the enhancement of the magnitude of Qst.170 These exchange reactions can also be a useful way to prepare new framework structures, especially if direct synthesis and activation of a particular materials proves challenging.171,172 In relation to H2 storage, a simple strategy was proposed and demonstrated in 2007 to improve the H2 adsorption properties of the framework Mn-BTT.173 In this work, metal cation exchange of the Mn-BTT structure resulted in successful isolation of the frameworks M3[(Mn4Cl)3(BTT)8]2 (M = Li+, Cu+, Fe2+, Co2+, Ni2+, Cu2+, Zn2+). The surface area of the series of metal-exchanged materials was slightly lower than the parent Mn-BTT structure, although a slightly larger Qst value was observed for Co3[(Mn4Cl)3(BTT)8]2 compared to Mn3[(Mn4Cl)3(BTT)8]2 (−10.5 versus −10.1 kJ mol−1, respectively). Based on the computational study of the aluminosilicate zeolite ZSM-5, it has also been proposed that Cu+-exchanged materials can exhibit strong H2 binding, although it was not possible to prepare a Cu+-rich M-BTT material.173,174 In 2014, Cu+ sites were introduced into the MFU-4l-type material Zn5Cl4(BTDD)3 (H2BTDD = bis(1H-1,2,3-triazolo[4,5-b],[4′,5′-i])dibenzo[1,4]dioxin) by a three-step, post-synthetic reaction, and the structure of the resulting material, Cu(I)-MFU-4l, was determined by X-ray diffraction.175 In this procedure, two Cu2+ ions in the metalated Cu(II)2Zn3Cl4 cluster were treated with lithium formate to yield Cu(II)-MFU-4l-formate [Cu(II)2Zn3Cl2(BTDD)3(formate)2], which was heated under vacuum to yield exposed Cu(I) sites. Hydrogen isotherm measurements revealed a 1:1 binding of H2 to the Cu(I) sites (corresponding to an uptake of 0.34 wt%) over the temperature range of 163–193 K, and 80% of the metal sites were found to be occupied by H2, even at 273 K and 1 bar. From H2 adsorption measurements, the Qst value for Cu(I)-MFU-4l was estimated to be −32.3 kJ mol−1, which, to our knowledge, is the highest value reported to date for any MOF. We note that the strength of this interaction in this framework may in part arise due to back-donation of electrons from the Cu metal center to H2, as has been observed in Kubas-type complexes (see below). Although this binding strength falls beyond the target range of −15 to −25 kJ mol−1 considered to be optimal for ambient-temperature H2 storage with a maximum pressure of 100 bar,25,35 targeting materials that possess metal ions capable of such back-donation and simultaneously exhibit strong physisorption may be a promising strategy to enhance storage capacity.
As materials are further developed to meet the current DOE onboard hydrogen storage targets (Table 1), one challenge that remains is to increase the density of strong binding sites, such as open metal sites, within a given volume of framework space. It is possible that strategies such as engineering frameworks with shorter organic linkers and optimizing pore topology will promote progress toward this goal, but most likely new material concepts and synthetic chemistry will be necessary to meet the targets.176 For example, prior to being synthesized in the lab, promising novel or already known materials for post-synthetic metalation reactions could first be identified using computational screening tools as outlined in the section on usable gravimetric and volumetric capacities. This type of targeted synthesis could result in materials with strong binding sites within pore structures that also demonstrate efficient H2 packing.
Fig. 8 Crystal structure of W(CO)3(PiPr3)2(η2-H2) (left) and RuH2(PCy3)2(η2-H2)2 (right).179,182 Gray, red, pink, blue, dark red, and light pink spheres represent C, O, P, W, Ru, and coordinated H atoms, respectively. Hydrogen atoms of the triphosphine ligands are omitted for clarity. |
While the first Kubas complexes exhibited only a single side-on bound H2 ligand, later metal complexes were identified that could reversibly bind two H2 molecules without cleaving the H–H bond.182–185 One representative example is the complex RuH2(PCy3)2(η2-H2)2, the structure of which was elucidated by single-crystal X-ray diffraction (Fig. 8).182,183 In this complex the two bulky phosphine ligands are located trans to each other, similar to the Kubas complexes, although an equatorial coordination pocket results that is capable of binding two H2 molecules and two hydrides. The H–H bond distance of each η2-bound H2 was estimated to be 0.85 Å, a value that is again indicative of a strong interaction when compared to materials exhibiting more conventional H2 physisorption. As expected given this strong interaction, the Ru–H2(centroid) distance of ∼1.50–1.55 Å is significantly shorter than the metal–D2 distance of >2.2 Å determined for Ni2(m-dobdc) from neutron diffraction measurements.29
Despite binding two H2 molecules per metal, RuH2(PCy3)2(η2-H2)2 only coordinates 0.6 wt% H2. Alternatively, the incorporation of a dense array of Kubas-type metal centers within a MOF—e.g., low-spin, first-row transition metals such as Cr or Mn186,187 coordinated by phosphine-based linkers—might be a promising strategy for achieving high H2 uptake; such a pursuit would no doubt be aided by computational screening of candidate framework structures. While the strength of the M–H2 bond dissociation energy in such compounds could reduce material usable capacity and cyclability, it is possible that designing Kubas-type sites within a flexible frameworks could offset this effect.
Fig. 9 (left) Crystal structure of Mn2(dsbdc)(DMF)2.189 (right) Coordinated DMF molecules (light blue) are removed to create exposed Mn2+ centers (green spheres), which adsorb two D2 molecules at a loading of 0.7 D2 per four-coordinate Mn2+ (at 10 K). Gray, red, yellow spheres represent C, O, and S atoms, respectively; H atoms are omitted for clarity. The coordination spheres of each Mn center are shown as blue and green polyhedra and D2 molecules are represented by orange spheres.134 |
The framework Zn2(dobdc) (UTSA-74a) is another material exhibiting two accessible binding sites that was recently studied for C2H2/CO2 separations.190 The as-synthesized, solvated framework exhibits a binuclear secondary building unit consisting of tetrahedral and octahedral Zn2+ ions. The coordination sphere of the octahedral Zn2+ is completed by two trans water molecules, which can be removed to yield a slightly distorted ZnO4 unit as observed by single crystal X-ray diffraction analysis. In the same study, DFT calculations predicted that the ZnO4 unit can accommodate two C2H2 adsorption sites at high loadings, a result that may have wider implications for the binding of other gases, including H2.
These recent reports afford valuable insight for continued optimization of framework design, although precise control over the inorganic unit remains a challenge. One alternative strategy for accessing open metal sites is to design ligands exhibiting secondary coordination sites that can be selectively metalated following framework synthesis.191 When compared with the direct synthesis of frameworks using pre-metalated linkers (e.g., metalated porphyrin or salen linkers),192–194 post-synthetic metalation is also potentially advantageous for accessing a wide variety of chelating moieties and metal ion combinations, although it is important to note that in some cases the protection of chelating sites is required during initial framework synthesis. One of the earliest examples of a framework prepared via post-synthetic metalation was reported in 2005, wherein the 1,1′-bi-2-naphthol moiety of the framework CdCl2(DCDPBN) (DCDPBN = 6,6′-dichloro-4,4′-di(pyridin-4-yl)-[1,1′-binaphthalene]-2,2′-diol) was metalated with titanium isopropoxide.195 Following this report, additional frameworks exhibiting 2,2′-bipyridine and salicylate sites were successfully metalated, and some of the resulting materials exhibited enhanced gas adsorption properties compared with the bare parent frameworks.196,197 However, metalation of neutral chelating groups resulted in pore-confinement of the counter anions and consequently diminished porosity and reduced accessibility of H2 to the metal center.
Another approach is to utilize organic linkers with catecholate sites, which can offer charge-balance for post-synthetically chelated divalent metal ions and obviate the need for countercations that would diminish porosity and capacity. The successful synthesis and subsequent metalation of a framework with catechol groups was first reported in 2010 by Tanabe et al.198 In this work, the authors prepared the framework Zn4O((OBnNO2)2-BDC)(BTB)4/3 (or nitrobenzyl-protected UMCM-1, (OBnNO2)2-BDC2− = 2,3-bis((2-nitrobenzyl)oxy)-1,4-benzenedicarboxylate, BTB3− = 4,4′,4′′-benzene-1,3,5-triyl-tribenzoate),199 which exhibits nitrobenzyl-protected BDC linkers. The nitrobenzyl groups could be removed by irradiation with 365 nm light, and the resulting catechol-functionalized UMCM-1 was then reacted with an iron(III) acetylacetonate solution to impregnate the framework with Fe3+ metal ions. Similar reactions have been carried out using Cr3+ and V4+ salts, which demonstrate the wide applicably of post-synthetic metalation reactions.200,201 These latter metalated frameworks were studied only for their utility in oxidative catalysis, however, and thus further efforts are necessary to examine the H2 affinity of metal-catecholate sites.
The interaction of H2 with some metal-catecholate clusters has been predicted computationally, and it was found that the H2 adsorption enthalpy exceeds that of metal-biphenol or metal–bipyridine complexes.59,60 For example, it was calculated that Mg2+ and Ca2+ catecholate complexes would exhibit H2 adsorption energies of 23.0 and 15.1 kJ mol−1, respectively, compared to the differential adsorption energies ΔE = 4.7 and 5.5 kJ mol−1 for biphenyl-(TiO4)-Me2 and bipyridine-CuCl2.60 The significant enhancement of the adsorption enthalpy can be attributed to the strong dipole moment created by the negatively charged oxygen atoms and positively charged metal ion—in other words, a local polarization interaction is critical to increase the binding energy of H2. It should be noted that the predicted M–H2 interaction energies for the Mg2+ and Ca2+ catecholate complexes are much lower than the H2 binding enthalpies determined for Kubas complexes (∼80 kJ mol−1) because of the absence of back-bonding from the alkaline-earth metal ions to H2, and these values are within a more optimal range for ambient temperature H2 storage. Importantly, within a UiO-66-type structure, it was predicted that Ca2+–catecholates are able to bind up to four H2 molecules per metal site without significant differences between the successive adsorption energies, resulting in a high calculated H2 volumetric usable capacity of 30 g L−1 at 298 K (pressures ranging from 5.8–100 bar).59 Therefore, the development of successful experimental protocols for the metalation of catechol-based frameworks (including the successful desolvation of any coordinated solvents) should be a key target for synthetic chemists.
A major advance in the chemistry of porous organic polymers came in 2009 with the discovery of high hydrothermal stability and exceptional surface area in the material PAF-1 (PAF = porous aromatic framework), a robust framework synthesized via a homo-coupling reaction with the tetrahedral building block tetrakis(4-bromophenyl)methane (Fig. 10).204 This material exhibits a high BET surface area of 5600 m2 g−1 (Langmuir surface area = 7100 m2 g−1) and excess gravimetric H2 uptake of 7.0 wt% at 77 K and 48 bar. Shortly after this report, several isoreticular organic frameworks were synthesized using larger tetrahedral building blocks.205,206 Among these materials, the framework known as PPN-4 (assembled using the tetrakis(4-bromophenyl)silane building unit) was found to possess a remarkably high BET surface area of 6461 m2 g−1 (Langmuir surface area = 10063 m2 g−1) and excess H2 adsorption as high as 8.3 wt% at 77 K and 55 bar.206 Porous organic frameworks can also be accessed using tritopic and tetratopic building blocks, as was demonstrated with the isolation of the framework JUC-Z7, assembled from tetrakis(4-bromophenyl)methane and tris(4-bromophenyl)amine. This material also exhibits high porosity, with a BET surface area of 4889 m2 g−1 and excess gravimetric H2 uptake of 6.4 wt% at 77 K and 48 bar (−Qst = 5.6 kJ mol−1).207 It should be noted that, similar to other high surface area materials mentioned previously, these materials do not exhibit high volumetric storage capacities due to their very large pores.
Fig. 10 Schematic representation of the synthesis of PAF-1 (top) and COF-102 (bottom).204,208 Gray, red, and orange spheres represent C, O, and B atoms, respectively; quaternary carbon atoms are shown as grey tetrahedra and H atoms of the triphosphine ligands are omitted for clarity. |
At least two challenges must be addressed to improve the H2 storage capacity in porous organic frameworks. The first challenge is the generally low experimental surface areas (typically <1500 m2 g−1) exhibited by porous organic frameworks, relative to expected values, especially for those materials exhibiting additional functionality. The formation of an interpenetrated structure is one likely source of low porosity, which can result from π–π interactions between neighboring frameworks and/or monomeric building blocks.209,210 Recent theoretical studies suggest these π–π interactions can be mitigated by replacing monomer phenyl and alkyne groups with rigid alkyl groups, while introducing bulky side chains into the framework structures may additionally increase the probability of forming dense frameworks.211 In the same work it was also proposed that interpenetrating structures could be avoided by the use of bulky coupling catalysts with dimensions similar to the target framework pore diameter.
A second challenge inherent in using porous organic frameworks for H2 storage is that these materials are only weakly polarizing and thus do not strongly bind H2. As discussed above in the context of MOFs, post-synthetic metalation of porous organic frameworks is one possible strategy for improving H2 binding energy. Successful pre- and post-synthetic metalation reactions have been demonstrated for a limited numbers of porous organic polymers exhibiting bipyridine, salen, porphyrin, and catechol chelating moieties.212–215 For instance, Weston et al. prepared catechol-functionalized porous polymers that could be cleanly metalated with MgMe2, Cu(CH3CO2)2, or Mn(CH3CO2)2, as demonstrated using IR spectroscopy.215 Metalation with Mn2+ afforded a material that exhibited an increase in Qst relative to the parent framework (−9.6 and −8.1 kJ mol−1, respectively), although it was not clear if this enhancement was directly related to the metalation. Fischer et al. have alternatively demonstrated that an anionic framework can be utilized to immobilize metal cations, through successful synthesis of a Li+-decorated borate-based porous polymer via coupling of lithium tetrakis(tetrafluorophenyl)borate and triethynylbenzene.216 The resulting material was found to exhibit moderate porosity, with a surface area of 890 m2 g−1 that was retained upon exchange of Li+ with Na+ or Mn2+ cations (surface areas of 731 and 499 m2 g−1, respectively). Future work would benefit from the investigation of the relationship between metal ion coordination environment and H2 adsorption in such materials.
Covalent organic frameworks are generally thermally and structurally robust, and activated samples can therefore be prepared without loss of crystallinity. The surface areas of activated COFs have been evaluated by both N2 and Ar adsorption analysis, and the reported values vary widely depending on the framework structure. For example, the two-dimensional materials COF-6 (prepared from the condensation reaction of hexahydroxytriphenylene and 1,3,5-benzenetriboronic acid) and CTF-1 (prepared from the condensation reaction of 1,4-dicyanobenzene) were found to exhibit BET surface areas of 750 and 791 m2 g−1, respectively, whereas the BET surface areas for three-dimensional frameworks COF-102 and COF-103 (prepared from the self-condensation reactions of tetra(4-(dihydroxy)borylphenyl)methane and tetra(4-(dihydroxy)borylphenyl)silane, respectively), were calculated to be 3620 and 3530 m2 g−1.208,220,224,225 As expected, COF-102 and COF-103 exhibit high excess gravimetric H2 uptakes (6.8 and 6.6 wt%, respectively) at ∼35 bar and 77 K, although their initial Qst values are only −3.9 and −4.4 kJ mol−1, respectively, due to a lack of strong H2 binding sites.225 Two-dimensional COFs such as COF-10 (prepared from the condensation reaction of hexahydroxytriphenylene and 1,4-benzenediboronic acid) and BLP-2(H) (obtained from the thermal decomposition of 1,3,5-(p-aminophenyl)benzene-borane) have been found to exhibit rather moderate saturation excess uptakes of 3.8 and 2.5 wt% at 77 K, relative to three-dimensional variants and the porous polymers described above.221,225 Importantly, the Qst values for two-dimensional COFs with similar pore diameter do not appear to be drastically influenced by the identity of linking moieties. For instance, changing from boronate (COF-6) to borazine (BLP-2(H)) to azine (ACOF-1; prepared by a condensation reaction of hydrazine hydrate and 1,3,5-triformylbenzene) resulted in frameworks with Qst values of −7.0 kJ mol−1, −6.8 kJ mol−1, and −6.0 kJ mol−1, respectively.221,225,226 The similarity of these values may be due in part to the fact that only the edge of each two-dimensional layer is exposed for interactions with H2 molecules, and suggests that such COFs are not ideal materials for practical H2 storage.
Although the impregnation of covalent organic frameworks with metal ions or metal particles could in principle lead to enhanced H2 storage capacities, this area of synthetic research has not been widely explored. To date, frameworks have been constructed with metalloporphyrin linkers or doped with Pd(CH3CO2)2, molybdenyl acetylacetonate, or various metallocenes.227–231 In one of the latter examples, COF-102 was impregnated with Pd(η3-C3H5)(η5-C5H5) and then photo-decomposed to yield Pd nanoparticles in the pores. The H2 uptake of the resulting material Pd@COF-102 was found to be slightly lower than that of pristine COF-102 at 77 K; at 298 K and 20 bar, however, the H2 uptake was 2.6 times greater than the pristine sample (0.42 compared to 0.16 wt%, respectively) due to the additional chemisorption of H2 on Pd.231 While frameworks doped with Pd(CH3CO2)2 and molybdenyl acetylacetonate were investigated for applications in catalysis, H2 adsorption characterization was not reported for any frameworks other than Pd@COF-102. We note that the presence of electron-deficient metal sites in these materials, arising from the electron withdrawing nature of the coordinated groups, could be of relevance for future study in pursuit of materials for H2 storage.
More recently, Klechikov et al. evaluated the H2 adsorption properties of various graphene and graphene oxide materials prepared via rapid thermal exfoliation and post-exfoliation activation treatments, which enabled them to systematically study the dependence of H2 uptake versus surface area.236 The authors found that H2 uptake by graphene materials does not exceed 1 wt% at 120 bar H2 at ambient temperatures; however, uptake at 77 K increases linearly as a function of material surface area, and a maximal H2 uptake of ∼5 wt% was observed for a graphene with a surface area of 2300 m2 g−1 (roughly following Chahine's rule behavior).10 The authors concluded that bulk graphene samples follow the standard H2 uptake trends of other nanostructured carbons and do not demonstrate intrinsically superior capacities; thus, unmodified graphene-based materials are essentially weakly-binding adsorbents.
Recently, Kim et al. studied the H2 adsorption properties of aggregated mesoporous graphene oxide intercalated with potassium ions, with the goal of demonstrating experimentally—in two dimensions—the thermodynamic principle that the density of H2 in a potential well increases exponentially relative to the ambient gas by the corresponding Boltzmann factor.234 The authors reported a gravimetric H2 storage density of 4.65 wt% at 40 bar and room temperature for this material, although in the absence of potassium ions they found the material exhibits a storage density of 0.21 wt% at ∼5 bar. The exceptional H2 uptake was rationalized as arising from the attractive potential of the mesopores and the intercalated potassium ions and, if accurate, would be the highest value reported for any adsorbent at ambient temperature; however validation of this result is needed by means of more comprehensive isotherm measurements on bulk samples beyond the quartz-crystal microbalance method used in the study. Further characterization of these materials should also be carried out to rule out the type of undesired side reactions that result in erroneously high capacities described above for materials containing surface oxides or reactive groups.
The malleable nature of graphene offers another potentially valuable route for the preparation of high-capacity H2 adsorbents, for example, Zhu and Li have proposed a hydrogenation-assisted graphene origami for hydrogen storage.233 Using MD simulations, the authors showed that a origami nanocage—which can be converted between open or closed configurations via an external electric field—could obtain a gravimetric capacity up to 9.7 wt%. Such a concept, although interesting, has yet to be experimentally verified.
A few experimental and theoretical studies have recently reported that enhanced H2 uptake can be achieved by metal atom doping of graphene surfaces. For example, Beheshti et al. predicted that double-sided Ca-decorated graphene doped with 12 atomic% of individual boron atoms can theoretically achieve a gravimetric H2 capacity of 8.38 wt% with an average binding energy of ∼38.6 kJ mol−1.237 Lee et al. similarly reported a first-principles study on hydrogen adsorption over Ca-decorated zigzag graphene nanoribbons (ZGNR), which predicted that each Ca atom is capable of binding up to six H2 molecules at a binding energy of ∼19.3 kJ mol−1 of H2, leading to a H2 gravimetric capacity of ∼5 wt%.87 However, both studies employed a relatively low level of DFT, which, as discussed above, is not always consistent with higher levels of theory (e.g., QMC calculations), and so these values should perhaps be interpreted with caution. Moreover, the synthesis of such adsorbents with low-coordinate dopant metal atoms that can accommodate several H2 molecules is likely to be extremely difficult, and has yet to be demonstrated. Nevertheless, some metal-doped carbons have been shown experimentally to exhibit improved storage properties; for example, Chen et al. synthesized a Pd-doped two-dimensional graphene sheet mixed with an activated carbon receptor and experimentally found a 49% enhancement in H2 gravimetric capacity and a higher Qst compared to the undoped mixtures at ambient temperature.238 In contrast to metal-site H2 adsorption predicted by the above theoretical studies, these enhancements were attributed to spillover effects. Zhou et al. have also reported a Ni–graphene composite containing nanocrystalline nickel particles uniformly dispersed over a graphene substrate, which exhibited room temperature gravimetric H2 capacities of 0.14 wt% at 1 bar and 1.18 wt% at 60 bar, respectively.239
Other graphene derivatives of interest involve new topologies such as carbon nanotubes and porous aromatic sp2 frameworks. Since the work by Dillon et al., which reported excellent H2 uptake by carbon nanotubes, extensive research has been conducted on hydrogen storage applications using carbon materials such as nanotubes and graphene derivatives.240 Despite initial enthusiasm, however, the reported performance by carbon nanotubes has been challenging to reproduce and architectures composed of undoped nanotubes are not a promising class of materials for practical storage applications.241 On the other hand, with the emerging aforementioned porous materials, other types of three-dimensional graphene architectures have been developed for H2 storage. Although various approaches to meeting the large storage capacity demands under ambient conditions have been proposed, the weak interactions between graphene materials and H2 molecules remain a daunting hurdle. Synthetic challenges surrounding metal doping of these structures still exist, including imparting precise control over the species present upon metal insertion, the degree of metal doping, and reversibility of H2 adsorption at these sites. Regardless, these materials display some potential towards ultimately meeting DOE targets if such challenges can be overcome.
Fig. 12 Structural model illustrating inclusion of one (a) or six (b) boron atoms in a fullerene and their interaction with molecular H2; green, blue, and white spheres represent C, B, and H atoms, respectively. Reprinted Fig. 1 and 4 (adapted) with permission from Y.-H. Kim, Y. Zhao, A. Williamson, M. J. Heben and S. B. Zhang, Phys. Rev. Lett., 2006, 96, 016102. Copyright 2016 by the American Physical Society. |
As a consequence of these promising theoretical studies, a number of experimental approaches have been explored to synthesize boron doped carbon materials with high surface areas and tunable porosity. In one of the first studies, B- and N-doped microporous carbons were synthesized via substitution reactions.243 The resulting doped graphite sheets were found to exhibit much higher surface areas and 53% higher H2 storage capacity than the pure carbon materials at room temperature. However, subsequent investigations of similar materials found little enhancement of H2 binding energy or storage capacity. This discrepancy between the computational predictions and the experimental observations is likely due to the difficulty of achieving experimentally the same boron environment that is modeled in the calculations; for example, the boron atom in the above fullerene calculations has a unique BC3 (sp2) non-planar, trigonal geometry, it is difficult to realize the same geometry by doping boron into planar graphitic structures. Other early experimental studies attempted to dope carbon with boron using anhydrous boric acid, but this approach provided little control over the doping site or the final functionality. In an attempt to address this synthetic challenge, Chung et al. used a specific class of boron-containing polymeric precursors with known connectivity to achieve a controlled approach to incorporating boron.27 Pyrolysis of the precursors resulted in relatively high surface area carbon materials (780 m2 g−1) with high boron content (7.2 wt%) and an H2 binding energy of 11 kJ mol−1. The substitutional p-type boron dopant was proposed to polarize the carbon surface, resulting in a binding energy higher than that achieved with neat carbon but lower than predicted for boron-doped fullerene structures.
The authors further used 11B magic angle spinning (MAS) NMR to gain insight into the boron environment in the carbon framework (Fig. 13).27 Deconvolution of the spectra of several B-doped carbon materials obtained at different pyrolysis temperatures revealed two components (best illustrated in the pale blue curve in Fig. 13b): one downfield arising from boron sites of trigonal planar symmetry, and one upfield corresponding to boron sites in a puckered configuration (Fig. 13c).
Chung and Jeong subsequently developed an alternative approach to prepare a range of porous boron-doped carbon materials, via pyrolysis of polymeric boron precursors in the presence of pore-templating LiCl or NaCl.244 Annealing at temperatures ranging from 600–1800 °C resulted in a range of structures, from those exhibiting minimal π conjugation and a boron-puckered configuration (600–800 °C) to more ordered structures with extensive π conjugation and a planar configuration (1500 °C). The planar graphitic layers were reported to accommodate <3 mol% B, while the amorphous materials exhibited much higher surface areas (500–800 m2 g−1) and 12 mol% B. The report claimed experimentally derived binding enthalpies of 12.5 and 20 kJ mol−1 for two structures, albeit with low capacities due to the small surface areas of the materials.
Tour and coworkers have alternatively used a bottom-up, solvothermal synthesis approach to prepare boron-, nitrogen-, and phosphorus-doped carbon scaffolds with surface areas as high as 900 m2 g−1, via the reaction of chlorine-containing organic molecules with metallic sodium at reflux in high boiling solvents, followed by the addition of heterotopic electrophiles for dopant incorporation.245 Hydrogen adsorption data for each material exhibited the expected type I isotherm behavior (Fig. 14), and heats of adsorption extrapolated to zero-coverage afforded Qst values of 8.6 and 8.3 kJ mol−1 for boron- and phosphorus-doped carbons, respectively. These values are notably higher than typical binding energies of 4–6 kJ mol−1 for undoped carbons, although the nitrogen-doped material was found to have a binding energy of 5.6 kJ mol−1, within this range.
Further experimental and computational work is underway to more precisely quantify the increased enthalpy of adsorption exhibited by these materials as well as to understand how boron modifies the graphitic carbon surface. Trigonal boron is more stable in a planar rather than puckered geometry, as the former enables more efficient electron donation to the electron-deficient boron atom. As such, a defect is generated when boron is substituted into a non-planar carbon matrix, and the nature of this defect may lead to an enhanced H2 binding energy to the carbon matrix. However, the lack of a reproducible value for the H2 binding energy in such materials presents a roadblock to their serious inquiry for H2 storage, and whether the variability in reported values is a reflection of synthetic difficulties or measurement complications remains unclear. Ultimately, any binding energy advantages achieved from boron (or other heteroatom) doping must also be accompanied by the ability to incorporate such sites into carbons with sufficient surface areas and porosities that can accommodate high H2 capacities.
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