Xiao-Dong
Li
*a,
Jing-Hua
Guo
b,
Hong
Zhang
*c,
Xin-Lu
Cheng
d and
Xiu-Ying
Liu
a
aCollege of Science, Henan University of Technology, Zhengzhou 450001, China. E-mail: dragoninstream@gmail.com
bSchool of Physics Science, University of Jinan, Jinan 250022, China
cCollege of Physical Science and Technology, Sichuan University, Chengdu 610065, China. E-mail: hongzhang@scu.edu.cn
dThe Institute of Atomic and Molecular Physics, Sichuan University, Chengdu 610065, China
First published on 13th May 2014
A new type of 1,3,5,7-tetraphenyladamantane-based covalent organic framework (adm-COF) was designed under the ctn and bor net topology with the method of molecular mechanics. The computed results reveal that all four designed adm-COFs exhibit extremely high porosity (86–95%) and large H2 accessible surface area (5967–6709 m2 g−1). The grand canonical Monte Carlo method was employed to simulate the adsorption isotherms of H2 gas in these adm-COFs at 77 K and 298 K. The simulated results indicate that, at 77 K and 100 bar, adm-COF-4 has the highest gravimetric H2 adsorption capacity of 38.36 wt%, while adm-COF-1 has the highest volumetric H2 adsorption capacity of 60.71 g L−1. Impressively, the gravimetric H2 adsorption capacity of adm-COF-1 can reach up to 5.81 wt% under 100 bar at room temperature, which is very close to the criterion of 6 wt% for the practical application of hydrogen at room temperature set by the U.S. Department of Energy. In addition, possible schemes for synthesizing these adm-COFs have been proposed.
Covalent organic frameworks (COFs) are one type of emerging porous crystalline architecture with two-dimensional (2D) or three-dimensional (3D) structures constructed by strong covalent bonds between light elements such as C, H, O, B, N, and Si.19–22 COFs have large pore volumes, high surface areas, and very low density,19 all of which are advantageous for gas storage. Therefore, many investigations have been performed to study the hydrogen storage properties of COFs or their modified counterparts.2,12,23–26 At the same time, many novel COFs have been reported either by experimental synthesis or by theoretical design.2,27–29 For example, Furukawa and Yaghi measured experimentally the H2, CH4, and CO2 adsorption isotherms on a series of COFs at 1–85 bar and 77–298 K.23 They well described the gas uptake behavior and capacity of these COFs by classifying them into three groups based on their structural dimensions and corresponding pore sizes. Mendoza-Cortes et al. calculated the H2 uptake at 298 K for several Li-, Na-, and K-metalized COFs by combining quantum mechanics calculations and grand canonical Monte Carlo (GCMC) simulations.24 Compared with their pristine counterparts, these metalized COFs possess enhanced hydrogen storage capacity at the studied condition. Additionally, Klontzas et al. studied hydrogen storage properties of four theoretically designed 3D COFs.27 Better yet, gravimetric uptake of one of these new COFs can surpass the value of 25 wt% at 77 K and reach the U.S. DOE's target of 6 wt% at room temperature. Using similar methods, Mendoza-Cortes et al. designed fourteen new COFs that can adsorb large amounts of methane up to 300 bar at 298 K.28 Also, by inserting pyridine molecules into the 2D COF-1 layers, Kim et al. proposed several pillared COFs (PCOFs) to expose buried framework surfaces to pores.29 With this approach, the PCOFs have significantly improved gravimetric and volumetric hydrogen storage capacities of 8.8–10.0 wt% and 58.7–61.7 g L−1, respectively.
Probing into the net topologies of 3D COFs,19 we find that the 3D COFs are mainly constructed through ctn or bor topology30 with tetrahedral and triangular building units. Typically, COF-102, COF-103, and COF-105 have ctn topology while COF-108 possesses bor topology, and, furthermore, COF-105 and COF-108 contain the same build units but different topology structures. The theoretically designed 3D COFs also conform to these two net topologies with various build units.27,28 Motivated and inspired by these studies, we designed four novel 3D porous covalent frameworks based on two planar triangular units appearing widely in 3D COFs19 and one tetrahedral building unit (1,3,5,7-tetraphenyladamantane) shown in Fig. 1. 1,3,5,7-tetraphenyladamantane is a rigid tetrahedral building block with similar geometry characteristics31,32 to tetraphenylmethane which appears frequently in the structures of 3D COFs in experiments.19,22 In a previous study,32 Schilling et al. synthesized a series of rigid tetrahedral organic building units from tetraphenylmethane and 1,3,5,7-tetraphenyladamantane precursors through Suzuki–Miyaura and Sonogashira cross-coupling reactions. Furthermore, adamantane-based tetrahedral units have been widely used for synthesizing various nanostructures.33–36 In one of our previous works, we also designed three types of adamantane-based aromatic frameworks with extremely high hydrogen storage capacity.37 However, to the best of our knowledge, there is no report on 1,3,5,7-tetraphenyladamantane-based crystalline porous COFs. Hence, in the present work, we designed four types of 1,3,5,7-tetraphenyladamantane-based COFs (adm-COFs) with ctn or bor net structures and investigated their hydrogen storage properties.
After the construction of the adm-COFs, we optimized them using the Forcite Plus module in Material Studio. The Dreiding force field39 and the ‘‘Ultra-fine’’ criterion are used for structural optimization. During the optimization, no space group symmetry constraints were imposed on the frameworks and all the bond lengths, angles, and cell parameters were optimized to get the best framework structures. The geometries are optimized until the remaining atomic forces are less than 0.0001 kcal mol−1 Å−1 on each atom and the energy convergence criterion is chosen as 1.0 × 10−5 kcal mol−1 between two steps. Based on the optimized structures, the GCMC simulations were performed to obtain the hydrogen adsorption isotherms for the four porous frameworks. During the simulations, the van der Waals interactions between H2 molecules and the frameworks are treated as 12–6 Lennard-Jones (L-J) potential as shown in eqn (1). The potential parameters of the framework atoms were taken from the Dreiding force field of Mayo et al.,39 and the potential parameters of H2 molecules were from the work of Buch,40 where a united-atom model for the H2 molecule is employed. All the potential parameters used in the present work are presented in Table 1. The cross-interaction parameters between different types of atoms are calculated using the Lorentz–Berthelot mixing rules shown in eqn (2) and (3). In addition, the L-J interactions were calculated with a spherical cut-off value of 13 Å.
![]() | (1) |
σij = (σii + σjj)/2 | (2) |
![]() | (3) |
H2 | He | C | H | O | B | |
---|---|---|---|---|---|---|
σ (Å) | 2.956 | 2.64 | 3.473 | 2.846 | 3.033 | 3.581 |
ε/kB (K) | 36.7 | 10.9 | 47.856 | 7.649 | 48.156 | 47.806 |
The adsorption of H2 gas was calculated using Monte Carlo (MC) simulations in the grand canonical ensemble (μVT) with the code Music,41 where the chemical potential, temperature, and volume are constant. Chemical potentials were converted to fugacity with the Peng–Robinson equation of state.42 During the simulations, 2 × 2 × 2 supercells for all frameworks were adopted and the periodic condition was employed in all three dimensions. The frameworks were frozen during the simulations. The total number of MC steps in a typical GCMC simulation was 2 × 107. The first half steps were used for equilibration and the second half steps were used for ensemble average. One MC step consisted of three trivial moves of H2 molecules; namely, insertion of a new molecule, deletion of an existing molecule, or translation of an existing molecule. The veracities of the employed force field parameters and the simulation method were validated in our previous paper.37 In addition, the excess H2 adsorption amounts (Nexc) were calculated by eqn (4):
Nexc = Nabs − ρVp | (4) |
Here, Nabs is the absolute H2 adsorption amounts, ρ is the density of the H2 gas under the thermodynamics conditions studied and Vp is the pore volume of the adsorbent. The density of H2 gas under a given pressure and temperature was computed by the Peng–Robinson equation of state.42 Finally, the H2 adsorption amounts were converted to gravimetric or volumetric H2 adsorption capacities to obtain H2 adsorption isotherms under a certain temperature. The pore volumes of the porous materials were evaluated with the method proposed by Talu and Myers.43 They suggested that the pore volume of porous material could be estimated by the amounts of adsorbed helium molecules (Na) at low pressure (P) and room temperature (T0) with eqn (5):
Vp = NakBT0/P | (5) |
Additionally, the isosteric heat of adsorption of H2 molecules (Qst) was calculated with eqn (6):44
![]() | (6) |
Materials | a = b = c (Å) | Chemical formula | M (g mol−1) | Density (g cm−3) | V p (cm3 g−1) | S (m2 g−1) | Q st (kJ mol−1) | |
---|---|---|---|---|---|---|---|---|
77 K | 298 K | |||||||
adm-COF-1 | 33.20 | C408H336B48O48 | 6526.02 | 0.30 | 2.9095 | 6021.39 | 3.41 | 4.00 |
adm-COF-2 | 21.58 | C102H84B12O12 | 1631.51 | 0.27 | 3.2422 | 5967.89 | 3.70 | 4.34 |
adm-COF-3 | 49.25 | C696H432B48O96 | 10849.90 | 0.15 | 6.245 | 6709.18 | 2.38 | 3.02 |
adm-COF-4 | 32.13 | C174H108B12O24 | 2712.48 | 0.14 | 6.9571 | 6696.16 | 2.50 | 3.38 |
The pore size is an important index to judge the performance of porous materials. Based on the amounts of helium molecules adsorbed in these adm-COFs at a pressure of 0.1–1 bar and a temperature of 298 K, their pore volumes were calculated by eqn (5) and the results are presented in Table 2. It can be seen that the pore volume of the four adm-COFs follow the sequence adm-COF-1 < adm-COF-2 < adm-COF-3 < adm-COF-4, which is just opposite to the sequence of density. To gain a concrete image of porosity, the percent pore volumes of the four adm-COFs are evaluated, and they are 86.18%, 87.39%, 94.17%, and 94.51% for adm-COF-1 to adm-COF-4, respectively. Excitingly, the very high porosity of all four adm-COFs is comparable with those of COF-105 (88.22%), COF-108 (88.84%) and PAF-1 (77.60%),19,46,47 which are all high-porosity materials with excellent hydrogen storage properties. Besides the pore volume, the surface area is also a key factor for gas adsorption in porous materials. Herein, we estimate the surface area of the adm-COFs using the accessible surface areas. The accessible surface areas of the adm-COFs were computed by a numerical MC integration technique proposed by Frost et al.48 It was performed by “rolling” a probe H2 molecule with a diameter equal to the L-J σ parameter of a H2 molecule (2.958 Å). The probe was randomly inserted around the surface of each framework atom with a diameter equal to each of their L-J σ parameters one by one to test for overlap. The fraction of probes that did not overlap with other framework atoms was used to calculate the accessible surface area. Surface area estimated using this method is highly dependent on the probe size used for measurement, and calculating the surface area using a H2 probe molecule provides the amount of area accessible to H2 molecules. As shown in Table 2, the H2 accessible surface areas for the four adm-COFs follow the sequence adm-COF-2 < adm-COF-1 < adm-COF-4 < adm-COF-3. Ascribed to the larger triangular building unit, adm-COF-3 and adm-COF-4 have larger surface areas than adm-COF-1 and adm-COF-2. Additionally, since ctn topology net possesses more complicated net structures than bor topology net, adm-COF-1 (adm-COF-3) has a larger surface area than adm-COF-2 (adm-COF-4). Anyhow, all adm-COFs reported here are on a par with porous materials reported with the highest surface area. To our knowledge, the highest surface area reported for MOF materials is claimed for MOF-210, which has a Brunauer–Emmett–Teller (BET) surface area of 6240 m2 g−1 and a Langmuir surface area of 10400 m2 g−1.49 In addition, the highest surface area reported up to now for COF materials is 4210 m2 g−1 (BET) of COF-103.19 Also, PAF-1 has a very high BET surface area of 5600 m2 g−1 and a Langmuir surface area of 7100 m2 g−1.47 The H2 accessible surface areas of the adm-COFs (5968–6709 m2 g−1) listed in Table 2 testify that they are all porous materials with large surface area. The high porosity and large H2 accessible surface area of these designed adm-COFs point to good hydrogen storage properties of these porous materials.
The adsorption isotherms of H2 of the four adm-COFs from 0.1 bar to 100 bar at 77 K are shown in Fig. 2. As depicted in Fig. 2, both absolute gravimetric and volumetric H2 adsorption capacities of the four adm-COFs increase gradually with an increase of H2 pressure, while the excess H2 adsorption capacities reach their maximums at low H2 pressure. It can be seen in Fig. 2a that the absolute gravimetric H2 adsorption capacity of adm-COF-1 is higher than that of adm-COF-2 at P < 30 bar, whereas it is reversed at P ≥ 30 bar. While, for adm-COF-3 and adm-COF-4, the absolute gravimetric H2 adsorption capacity of adm-COF-4 is higher than that of adm-COF-3 at all pressures studied. The maximum absolute gravimetric H2 adsorption capacities are 20.66 wt%, 22.08 wt%, 32.87 wt% and 38.36 wt% for adm-COF-1, adm-COF-2, adm-COF-3 and adm-COF-4, respectively. At the same time, the maximum excess gravimetric H2 adsorption capacities are 10.60 wt% for adm-COF-1 at 30 bar, 12.80 wt% for adm-COF-2 at 40 bar, 12.08 wt% for adm-COF-3 at 70 bar and 15.13 wt% for adm-COF-4 at 70 bar. On the other hand, as depicted in Fig. 2b, the absolute volumetric H2 adsorption capacities for the four adm-COFs obey the sequence of adm-COF-1 > adm-COF-2 > adm-COF-4 > adm-COF-3, which is basically contrary to that of the absolute gravimetric H2 adsorption capacities. The maximum absolute (excess) volumetric H2 adsorption capacities are 60.71 g L−1 (36.93 g L−1 at 30 bar), 59.06 g L−1 (34.12 g L−1 at 40 bar), 49.18 g L−1 (17.88 g L−1 at 70 bar) and 51.70 g L−1 (20.21 g L−1 at 70 bar) for adm-COF-1 to adm-COF-4, respectively. All these results reveal that the adm-COFs have excellent hydrogen storage capacities at 77 K.
Since the practical application of hydrogen should be at room temperature, we also calculated the hydrogen uptake of the adm-COFs at 298 K. As can be seen in Fig. 3, both gravimetric and volumetric H2 adsorption capacities increase linearly with an increase of H2 pressure at 298 K. This is a characteristic of Henry's linear isotherm equation.50,51 Henry's linear isotherm equation is n = KP, where n is the adsorbed amount per unit weight of adsorbent (wt%), P is the adsorbate gas pressure at equilibrium (bar), and K is Henry's law constant (wt% per bar). The fitted linear isotherm equations for the four adm-COFs and their degrees of linear correlation are listed in Fig. 3a. The subscripts 1 to 4 in these equations denote the corresponding equations and degrees of linear correlation for adm-COF-1 to adm-COF-4. The excellent linearity reveals that the H2 adsorption capacity of these adm-COFs is proportional to the pore volume and virtually independent of binding energy or surface area at room temperature. As shown in Fig. 3, the gravimetric H2 adsorption capacities follow the sequence of adm-COF-1 < adm-COF-2 < adm-COF-3 < adm-COF-4 at all pressures studied, which is indeed the same sequence as the size of the pore volume from Table 2. In Fig. 3, the maximum absolute gravimetric (volumetric) H2 adsorption capacities are 2.73 wt% (8.03 g L−1), 2.98 wt% (7.98 g L−1), 4.65 wt% (6.96 g L−1) and 5.81 wt% (7.83 g L−1) for adm-COF-1 to adm-COF-4 at 100 bar, respectively. Surprisingly, the maximum gravimetric H2 adsorption capacities for adm-COF-3 and adm-COF-4 exceed the U.S. DOE's goal (4.5 wt%) for 2017.18 In particular, adm-COF-4 has a maximum gravimetric H2 adsorption capacity of 5.81 wt%, which approaches the capacity (6 wt%) for practical application of hydrogen at room temperature proposed by the U.S. DOE. However, it is a pity that the four adm-COFs all have low volumetric H2 adsorption capacity at room temperature, which again indicates the dependence of H2 adsorption capacity on the pore volume. To enhance the volumetric H2 adsorption capacity of these adm-COFs, some modified methods must be adopted, which are being carried out in subsequent studies.
![]() | ||
Fig. 3 The computed absolute H2 adsorption isotherms of the four 3D adm-COF frameworks at 298 K: (a) gravimetric H2 adsorption isotherms and (b) volumetric H2 adsorption isotherms. |
We have computed the isosteric heats of adsorption of H2 molecules of the four adm-COFs at both 77 K and 298 K by eqn (6). Table 2 lists the average isosteric heat of adsorption of H2 molecules for each adm-COF at 77 K and 298 K. It can be seen that adm-COF-1 and adm-COF-2 have larger average isosteric heat of adsorption of H2 than adm-COF-3 and adm-COF-4. This can be attributed to the smaller triangular units of adm-COF-1 and adm-COF-2, which introduce smaller cavities than adm-COF-3 and adm-COF-4 and hence produce stronger van der Waals interactions between the H2 molecules and the frameworks. On the other hand, due to the different net topologies of the four adm-COFs, adm-COF-2 (adm-COF-4) with bor topology can adsorb H2 molecules with larger average isosteric heat of adsorption than adm-COF-1 (adm-COF-3) with ctn topology. In addition, it needs to be pointed out that isosteric heats of adsorption for H2 molecules in the four adm-COFs are all very small. Some previous work has pointed that a value of isosteric heat larger than 15 kJ mol−1 is likely to be needed for practical hydrogen storage.7 To improve the isosteric heats of adsorption of H2 molecules in adm-COFs, some modified methods can be adopted. This problem is consistent with the low volumetric H2 adsorption capacity at room temperature, which is discussed in the previous paragraph.
Furthermore, to understand the adsorption behaviors of H2 gas in the frameworks at a molecular level, we examined snapshots of the four adm-COF structures with adsorbed H2 molecules at both 77 K and 298 K. Snapshots of the four adm-COFs with adsorbed H2 molecules at 77 K and 100 bar are shown in Fig. 4. From these snapshots, we find that the triangular units, especially the B3O3 and BC2O2 rings, are the preferential adsorption sites for H2 molecules. During the adsorption process, the H2 molecules are first adsorbed on the triangular units at low H2 pressure. With an increase of the H2 pressure, the H2 molecules begin to occupy the corner sites near the tetrahedral units. At last, the H2 molecules accommodate the cavities far from the framework surface for further rise of H2 pressure.
![]() | ||
Fig. 4 The equilibrium snapshots of the four adm-COF structures with H2 molecules adsorbed under a pressure of 100 bar at 77 K: (a) adm-COF-1, (b) adm-COF-2, (c) adm-COF-3 and (d) adm-COF-4. |
Finally, we propose two possible schemes to synthesize these adm-COFs. We chose tetra(4-dihydroxyborylphenyl)adamantane (TBPA) as tetrahedral building unit (Fig. 5a) and hexahydroxytriphenylene (HHTP) as triangular building block (Fig. 5b). In principle, an infinite number of possible nets may result from linking tetrahedrons with triangles. However, analysis of previous assembly reactions suggests that the most symmetric nets are the most likely to result in an unbiased system, and that those with just one kind of link will be preferred and are thus the best to target.19 In the present case of linking tetrahedral and triangular building blocks, the only known nets meeting the above criteria are those with ctn and bor19,30 topologies, shown in Fig. 1. Based on these backgrounds, we propose the synthesis schemes (R1 and R2) for these adm-COFs, as depicted in Fig. 5. As shown in Fig. 5, adm-COF-1 and adm-COF-2 may be synthesized by self-condensation of TBPA to form B3O3 rings (Fig. 5c), while adm-COF-3 or adm-COF-4 can be obtained by co-condensation of TBPA and HHTP to form C2O2B rings (Fig. 5d). To form the 3D ctn and bor structures, the use of rigid, planar triangular units, such as B3O3 rings, requires that there be rotational freedom at the tetrahedral nodes.
Footnote |
† Electronic supplementary information (ESI) available: The space group symmetries and coordinates of these adm-COF materials are provided. See DOI: 10.1039/c4ra02988g |
This journal is © The Royal Society of Chemistry 2014 |