Open Access Article
This Open Access Article is licensed under a
Creative Commons Attribution 3.0 Unported Licence

Confined toluene within InOF-1: CO2 capture enhancement

L. Pamela Garrido-Olveraa, Jonathan E. Sanchez-Bautistaa, Daniel Alvarado-Alvaradoa, Bruno Landeros-Rivera*b, J. Raziel Álvareza, Rubicelia Vargas*b, Eduardo González-Zamorab, Jorge Balmasedac, Hugo A. Lara-Garcíad, Ana Martínezc and Ilich A. Ibarra*a
aLaboratorio de Fisicoquímica y Reactividad de Superficies (LaFReS), Instituto de Investigaciones en Materiales, Universidad Nacional Autónoma de México, Circuito Exterior s/n, CU, Coyoacán, 04510 Ciudad de México, Mexico. E-mail: argel@unam.mx
bDepartamento de Química, Universidad Autónoma Metropolitana-Iztapalapa, San Rafael Atlixco 186, Col. Vicentina, Iztapalapa, C. P. 09340 Ciudad de México, Mexico. E-mail: brunolanderos@hotmail.com; ruvf@xanum.uam.mx
cInstituto de Investigaciones en Materiales, Universidad Nacional Autónoma de México, Circuito Exterior S/N, CU, Coyoacán, 04510, Ciudad de México, Mexico
dInstituto de Física, Universidad Nacional Autónoma de México, Circuito de la Investigación científica S/N, CU, Del. Coyoacán, 04510, Ciudad de México, Mexico

Received 2nd August 2019 , Accepted 30th September 2019

First published on 15th October 2019


Abstract

The toluene adsorption properties of InOF-1 are studied along with the confinement of small amounts of this non-polar molecule revealing a 1.38-fold increase in CO2 capture, from 5.26 wt% under anhydrous conditions to 7.28 wt% with a 1.5 wt% of pre-confined toluene at 298 K. The InOF-1 affinity towards toluene was experimentally quantified by ΔHads (−46.81 kJ mol−1). InOF-1 is shown to be a promising material for CO2 capture under industrial conditions. Computational calculations (DFT and QTAIM) and DRIFTs in situ experiments provided a possible explanation for the experimental CO2 capture enhancement by showing how the toluene molecule is confined within InOF-1, which constructed a “bottleneck effect”.


Introduction

In the last decades, global warming has become one of the biggest threats that our civilization faces. Scientists agree that this phenomenon is related to the cumulative emissions in the atmosphere of carbon dioxide (CO2) and the increase of anthropogenic activities which generate the so-called greenhouse gases (GHG).1 According to the International Energy Agency (IEA)2 the energy industry is the sector with the highest CO2 emissions, resulting in 42% of the global total emissions in 2016. In spite of the current necessity for using renewable energy sources, and different efforts to develop new technologies, the production of energy from fossil fuel sources will, unfortunately, remain dominant for the coming years.

Undeniably, identifying present problems and working on multiple solutions to reduce the atmospheric CO2 levels is critical to mitigate the environmental threats and problems that global warming present. Sequestration of CO2 represents a promising method for mitigation, and a key step solution to effectively reduce the CO2 levels in ecosystems. However, in order to solve the problem of global warming and high concentration levels of CO2, the search and development for a cost-effective capture technology is needed. Several technologies and materials have been proposed to mitigate the emissions, for instance, the carbon sequestration of biomass feedstock, microalgae.3 On the other hand, Carbon Capture and Storage (CCS) are a wide group of technologies being developed in aim to capture and safely storage the CO2 emitted from industrial processes before it enters the atmosphere.4,5

Unfortunately, CO2 is not the only GHG which negatively contributes to affect the environment, but there is a vast list of chemical pollutants that are quite abundant in both the outdoor environment and indoor air quality.6 Volatile organic compounds (VOCs), and more specifically BTEX (benzene, toluene, ethylbenzene and xylene) are key materials in the organic chemistry industry. Organic chemicals are used in household products, which can release organic compounds when using them.7 Recent studies indicate that VOCs are considered a major group of air pollutants and a serious concern due to their major environmental and human health hazard.8

Multiple methods of gas capture materials are used at present for the sequestration for both CO2 and VOCs, from activated carbon to zeolites, calcium oxides, hydrotalcites, lithium zirconate, and metal–organic frameworks (MOFs).9

MOFs emerged as a promising alternative to solve various problems and to overcome limitations experienced with solid sorptive materials. The structure of MOFs consists of metal centers connected by organic ligands which results in a porous material with high surface area, diverse size of the cavities and thus, different applications have been found.10 Depending on the selection of the organic ligand and the metal centre, the resulting MOF material will have distinctive properties. As a result of this flexibility, MOFs sorption selectivity towards CO2 (in comparison to other gases e.g., CH4, N2 and H2), makes them one of the principal candidates for capture and separation of CO2.

Recent studies have demonstrated that the inclusion of different molecules, within nanometre scale materials induce an increase the gas solubility in which Henry's law might be limited.11 This phenomenon is also known as “gas-over solubility” and can modify the physicochemical properties of the confined molecules (typically solvents).12,13 Several research groups have reported an increase of gas solubility when relatively large amounts of molecules are pre-adsorbed in mesoporous solid materials. Luzar and Bratko predicted (Monte Carlo calculations) an increase on the solubility of different gases (O2, N2, CO2, and Ar) when water molecules are included in a hydrophobic environment.14,15 Pera-Titus et al., reported an enhancement on the H2 solubility when different molecules (i.e., CS2, CHCl3, CCl4, n-C6H14, H2O, and EtOH) were confined.13,16 In more recent studies it has been demonstrated that, in water stable MOFs, small amounts of pre-absorbed water (confined) within their pores, it can considerably enhance CO2 capture.17 Experimental data in different water stable MOFs such as InOF-1,18 NOTT-400,19 and Mg-CUK-120 allowed to elucidate the role of confined water molecules within these MOFs, and how the interactions (hydrogen binding) of water with the hydroxo functional groups (μ2-OH) are the key for the CO2 capture enhancement.17

Additionally, MOFs exhibit high capacity and selectivity for VOCs, as well as promising sorption and separation capacities.21 Regardless of the characteristics of some previously studied MOFs, their application as sorptive materials for the removal of VOCs (such as toluene) has been a challenging task. A vast group of capture methods have been investigated such as condensation, catalytic oxidation, biodegradation, and adsorption methods.22

InOF-1 is a water-stable microporous MOF material, which is constructed from a flexible BPTC (biphenyl-3,3′,5,5′-tetracarboxylate) and based on a binuclear [In22-OH)] building block.23 Sequestration of CO2 in InOF-1 has previously been demonstrated under anhydrous conditions and with the pre-adsorption (confinement of small amounts) of different polar molecules,24–28 resulting in the increase on the total CO2 capture. In all these examples the hydrogen bond between these polar molecules and the hydroxo functional group, showed to be the dominant intermolecular interaction to enhance the CO2 uptake. In this study we present the capture of CO2 with a pre-confined solvent that happens not to be a hydrogen bonding donator within the InOF-1 material: toluene. The CO2 capture properties of InOF-1 and the adsorption of toluene were experimentally studied and correlated with computational calculations.

Experimental details

Chemicals

Indium nitrate (In(NO3)3), biphenyl-3,3′,5,5′-tetra-carboxylic acid (H4BPTC), N,N′-dimethyl formamide (DMF), acetonitrile (CH3CN), and nitric acid (HNO3) were obtained from Sigma-Aldrich and used as received without any further purification. Water (H2O) and acetone (Me2CO), used for washing purposes, were technical grade.

Synthesis and activation

InOF-1 = [In2(OH)2(BPTC)] = In2(OH)2(biphenyl-3,3′,5,5′-tetra-carboxylate), was synthesised according to the previously reported procedure methodology by Hong et al.23 The precipitate is formed by dissolving In(NO3)3·5H2O (156 mg, 0.4 mmol), and H4BPTC (33 mg, 0.10 mmol) in DMF (5 mL), MeCN (5 mL), and HNO3 (0.2 mL, 65 wt%), in a sealed pressure tube. The clear solution is heated at a temperature of 85 °C (358 K) in an oil bath for 72 h. The pressure tube was cooled down to room temperature over a period of 12 h and the colourless crystalline product was separated by filtration, washed with DMF (5 mL), and finally dried in air leading to a yield of 73% (based on ligand). Powder X-ray diffraction (PXRD) analysis was performed on the InOF-1 sample to confirm the MOF structure and control the purity of the synthesised material. The as-synthesised sample was acetone-exchanged and then activated at 453 K (810 °C) for 2 h with a constant flow of dry N2 gas.

PXRD experiments

Powder X-ray diffraction (PXRD) analyses were performed in a Bruker AXS D8 Advance system (Cu Kα radiation) to confirm the purity of the synthesised material (see Fig. S1, ESI). PXRD patterns were recorded under ambient conditions from 5 to 55° (2θ) with a 0.02° per step, at a scan rate of 0.8° min−1. These patterns were obtained from the as-synthesised material and after the CO2 capture experiments.

Adsorption isotherms for toluene

To record the toluene sorption isotherms, ultrapure grade (99.9995%) N2 gas purchased from Praxair was used as a vapour carrier in a DVS Advantage 1 instrument, from Surface Measurement Systems (mass sensitivity: 0.1 μg; RH accuracy: 0.5% RH, vapor pressure accuracy: 0.7% P/P0). Toluene adsorption–desorption isotherms were collected at 308 and 298 K. InOF-1 samples were activated at 453 K for 2 hours under a dry N2 flow on the DVS prior to toluene adsorption experiments. In order to obtain the isotherms, a partial pressure method was carried out with controlled changes of partial pressure and a constant temperature in the sample chamber.

Kinetic CO2 uptake experiments

CO2 uptake experiments were performed in the same instrument from Surface Measurement Systems (vide supra) at constant temperature and CO2 flow. Prior to any CO2 uptake experiments, InOF-1 samples were fully activated by increasing the temperature to 453 K under a dry N2 gas flow for 2 h in the DVS Advantage 1 instrument. A selected partial pressure of 1.5% P/P0 was used to achieve the desired weight percentage of confined toluene within the activated sample of InOF-1. Then, CO2 uptake experiments were carried out at 298 K allowing a constant CO2 gas flow (100 cm3 min−1) inside the sample chamber until the sample mass remained constant.

Computational details

Density Functional Theory (DFT) periodical calculations of the toluene adsorption process, in InOF-1, were performed at B3LYP-D*/POB-TVPZ29,30 level of theory employing the Crystal14 software.31 The initial structure for the geometry optimisation present the toluene ring laying parallel over one of the biphenyl rings (ligand) of InOF-1. Toluene molecule was fully geometry optimised whilst the rest of the atomic positions and the cell parameters remained fixed. The intermolecular interactions were analysed by means of the quantum theory of atoms in molecules32 (QTAIM), the Non-Covalent Interaction index33 (NCI) and the electrostatic potential. The QTAIM analysis, as well as void volume computations based on an electron density isosurfaces, was conducted with a program developed by our research group that is in a beta version of GPUAM.34 The NCI analysis was performed over a pro-molecular density with the NCIPLOT program.35 Once the geometry of the toluene molecule was optimised, a CO2 molecule was placed over its aromatic ring and its positions were relaxed, keeping the rest of the system fixed. This computation was carried out using the same procedure stated above.

DRIFT spectroscopy

Diffuse Reflectance Infrared Fourier Transform (DRIFT) spectroscopy experiments were performed using an environmentally controlled PIKE DRIFT cell with SeZn windows coupled to a Thermo Scientific Nicolet iS50 spectrometer with a DTGS detector. Absorbance spectra were obtained by collecting 64 scans at 4 cm−1 resolution. A sample of 25 mg was pre-treated in situ under a helium flow of 30 mL min−1 at 180 °C for 1 h. After this treatment, the sample was functionalised with toluene (toluene@InOF-1). CO2 adsorption was studied using a flow of 30 mL min−1 of CO2 (5% CO2 in Ar). Spectra of the toluene-functionalised InOF-1 were collected at different times.

Results and discussion

Toluene sorption studies

Fig. 1 shows the toluene adsorption–desorption isotherm for InOF-1 carried out from % P/P0 = 0 to 85 at 298 K. Due to possible favourable host–guest interactions, the uptake rapidly rises with P/P0 (see Fig. 1). The toluene capture quickly increased attaining an uptake of approximately 13.9 wt% (1.5 mmol g−1) from 0 to 15% P/P0. The toluene uptake was clearly slower from 15 to 85% P/P0, with a maximum capture of approximately 16.5 wt% (1.8 mmol g−1). The desorption phase shows hysteresis more evidently at the low pressures ranges from 0 to 10% P/P0 (see Fig. 1). Thus, a high affinity of InOF-1 towards toluene is shown in the desorption phase. Once desorption is completed, a considerable amount of toluene remained trapped inside the pores of the material (approximately 9.6 wt%, 1.05 mmol g−1), which suggests a relatively strong host–guest interaction between toluene and InOF-1.
image file: c9ra05991a-f1.tif
Fig. 1 Toluene adsorption–desorption isotherm at 298 K of InOF-1 from 0 to 85 %P/P0.

In order to estimate the isosteric heat of adsorption (ΔHads) and to investigate the adsorbate–adsorbent interactions (see Fig S2, ESI) another toluene adsorption isotherm was carried out at 308 K. The isosteric heat of adsorption was calculated by fitting both adsorption toluene isotherms (298 and 308 K) to the Clausius–Clapeyron equation (see Fig. S3, ESI), resulting in a ΔHads = −46.81 kJ mol−1. The ΔHads value was higher than the molar enthalpy of vaporisation for toluene (ΔHvap = 38.01 kJ mol−1), which is consistent with previously reported 25,26,28values for other confined solvents in the same material, InOF-1 and within the range of previously reported MOFs with toluene sorptive capability.36

CO2 capture studies

Under anhydrous conditions and at 298 K, the maximum CO2 capture was estimated to be 5.26 wt%. This value is in agreement with previously reported CO2 captures at the same temperature.27 As shown in Fig. 2, after 12 min the mass gain remained essentially constant until the end of the experiment (at approximately 50 min). This means that the CO2 capture reached stability after approximately 12 min.
image file: c9ra05991a-f2.tif
Fig. 2 CO2 dynamic adsorption experiments performed at 298 K under for InOF-1 (red curve) and toluene@InOF-1 (blue curve); CO2 error ±0.05 wt%.

Intrigued by the high affinity of InOF-1 towards toluene (non-polar molecule) we decided to analyse the effect of pre-confining small amounts of toluene and investigate the effect on the CO2 adsorption properties of the hybrid material. Since toluene is a non-polar molecule, the formation of hydrogen bonds with the hydroxo functional group (μ2-OH) should be less possible. Therefore, the CO2 uptake should be approximately the same as under anhydrous conditions.

To verify this hypothesis, we decided to confine (pre-adsorb) a small amount of toluene (1.5 wt%) into the pores of InOF-1. In a DVS Advantage 1 instrument (SMS) with an isothermal and dynamic method, a partial pressure of toluene was selected (1 %P/P0) allowing the pre-adsorption of the non-polar molecule (with dry N2 acting as a carrier gas) within the pores of InOF-1. The mass increased to the expected weight percentage value (see Fig. 1), and when the toluene uptake remained constant at 1.5 wt%, the partial pressure was returned to 0% P/P0 maintaining the sample mass constant pre-adsorbing toluene within the pores of InOF-1. This sample was labelled as toluene@InOF-1. Then, a CO2 flow (100 cm3 min−1) was started and allowed into the sample chamber of the DVS instrument. The CO2 uptake for toluene@InOF-1 rapidly increased reaching a steady state after only 8 min and fully stabilised (plateau) at 10 min approximately. The maximum amount of CO2 captured for toluene@InOF-1 was equal to 7.28 wt% (see Fig. 2). This CO2 kinetic-uptake experiment demonstrated that the pre-confinement of 1.5 wt% of toluene within InOF-1 (toluene@InOF-1) resulted in a 1.38-fold CO2 increase capture (from 5.26 wt% to 7.28 wt%).

In order to corroborate the CO2 capture cyclability of toluene@InOF-1 (evaluation of the regeneration properties and the CO2 desorption process), six CO2 adsorption–desorption cycles were performed at 298 K. For this, isothermal and dynamic experiments at 298 K were performed in a DVS Advantage 1 instrument (SMS) without the use of any dry N2 or other gas as a purge. As shown in Fig. 3, each cycle involved an approximate 20 min adsorption step of CO2 followed by an ∼70 min CO2 desorption step, to complete a 600 min cycling (adsorption–desorption). By only turning off the CO2 flow (absence of a purge gas in the desorption step), only a partial regeneration of toluene@InOF-1 was achieved. Fig. 3 demonstrates that on each cycle the CO2 desorption step is reduced even more, with a total CO2 capture of 7.20 wt% in the first cycle and a desorption of 4.57 wt%. After six cycles the CO2 capture was equal to 7.28 wt% and a desorption of only 0.33 wt%. Remarkably, the capture capacity seems not to be affected by the number of cycles maintaining the maximum enhancement of CO2 of 7.28 wt%. This result is relevant since it shows not only an unexpected CO2 capture enhancement by the confinement of toluene, but also the retention of the CO2 cyclability of toluene@InOF-1 due to an extraordinary high affinity of InOF-1 towards toluene. In addition, it was corroborated by a PXRD experiment, the structure stability of the material after the CO2 adsorption–desorption cycling experiments (see Fig. S1, ESI).


image file: c9ra05991a-f3.tif
Fig. 3 Adsorption–desorption CO2 cycling for toluene@InOF-1.

Computational studies

In order to investigate more about (i) the affinity of InOF-1 to toluene and (ii) the unexpected CO2 capture enhancement of toluene@InOF-1, powerful periodical DFT and QTAIM calculations were carried out. DFT results shows that the toluene molecule is placed over one of aromatic rings of InOF-1 in a parallel displaced structure,37 i.e., both molecular rings are nearly parallel but their carbon atoms are not aligned in the perpendicular direction to the planes (see Fig. 4), with an average inter-planar distance of 3.17 Å. This bond length is an expected value for π–π stacking interactions. As it has been previously demonstrated, this type of interactions have a large dispersive component.38,39
image file: c9ra05991a-f4.tif
Fig. 4 Pore channel (top) and close up (bottom) views of the optimized structure of the toluene molecule (shown in blue) adsorbed within InOF-1 in a parallel displaced geometry. Pink, red, grey and white colours represent indium, oxygen, carbon and hydrogen atoms, correspondingly. This figure was generated with the Mercury software.40,41

Nevertheless, although the electrostatic energetic contribution performs a minor role, it has a strong influence on the orientation of the molecules. As can be seen in the electrostatic potential map (MEP) in Fig. 5, the parallel displaced configuration avoids contact between the negative regions (red colour) that are found in the carbon rings of toluene and the biphenyl moiety of InOF-1. Additionally, the MEP also suggests the presence of weak C–H⋯O hydrogen bonds, that can be induced by the contact between the positive areas around the hydrogen atom of toluene (blue colour) with the negative of the oxygen atom (red colour) of InOF-1. Another parallel structure was found with an interplanar separation of 3.339 Å (see Fig. S4, ESI), but it was not considered in this discussion since it is less stable by 8.1 kcal mol−1 and we focus our analysis in the most stable one. There is another geometric arrangement common in non-polar aromatic dimers, where both rings are placed in perpendicular planes42 (T-shaped structure). Notwithstanding, this structure was not considered because the toluene molecule could easily be displaced by a gas flux (e.g., CO2) since a larger contact area of the molecule (toluene) would be exposed and therefore, pushed out the pores of InOF-1.


image file: c9ra05991a-f5.tif
Fig. 5 Electrostatic potential of the parallel displaced structure of the toluene molecule adsorbed in InOF-1 over a ρ = 0.03 a.u. isosurface (blue 0.01 and red 0.10 a.u., respectively). Partial charges are depicted in yellow. This figure was created with the VMD program.43

A deeper understanding of the intermolecular interactions responsible for the toluene adsorption in InOF-1 can be acquired by the analysis of the electron density, ρ(r), and its derivatives. According to the quantum theory of atoms in molecules (QTAIM), the appearance of bond critical points (BCP) and bond paths (BP) indicates the existence of covalent, as well as non-covalent interactions associated to specific atom–atom contacts. In Fig. 6, the BCP and BP corresponding to intermolecular interactions between toluene and InOF-1 are depicted as orange points and tubes, respectively. In agreement with the previous analysis of the MEP, several type of non-covalent interactions where found: C⋯C, that are related to π-π stacking, C–H⋯O, which confirms the presence of this sort of weak hydrogen bond, and the controversial H⋯H contacts, whose nature and consequences are a matter of debate.44,45 The value of the electron density at the BCP, ρB, is proportional to the interaction strength. From Table S1, it is noted that the ρB values are around 10−3 a.u., which is an order of magnitude lower than those of strong intermolecular interactions such as an O–H⋯H hydrogen bond. Interestingly, an exception was found for a H⋯H contact (circled in black in Fig. 6) between one hydrogen atom of the aromatic ring of toluene and the hydrogen atom of the μ2-OH functional group of InOF-1 (ρB = 0.015 a.u.) at 1.812 Å. Even though π–π and C–H⋯O interactions were also found in the structure provided in the ESI (see Fig. S4, ESI), we propose that the H⋯H contacts are partially responsible for the energy difference of 8.1 kcal mol−1. This outcome highlights a new feature of this MOF material; the μ2-OH functional group of InOF-1 can contribute to the adsorption of non-polar molecules, albeit in a lower degree in comparison with effect it has in the interaction of polar molecules.24,27


image file: c9ra05991a-f6.tif
Fig. 6 Bond critical points and bond paths (orange points and tubes, respectively) denoting the intermolecular interactions between toluene (blue) and InOF-1. The H⋯H interaction is circled in black colour. This figure was created with the VMD program.43

Finally, by means of the NCI analysis it was possible to elucidate the nature of the present interactions. From the NCI isosurface (see Fig. 7), the existence of π–π stacking is confirmed by the green surfaces that indicates the presence of van der Waals forces between toluene and InOF-1.33 The C–H⋯O interactions are visualised by green flat-localised shapes (see Fig. 7) that are characteristic of very weak hydrogen bonds.41 The H⋯H contacts also exhibit green extended surfaces attributed to dispersive interactions, except for the one formed between toluene and μ2-OH (circled in red in Fig. 7). This contact displays a teal colour disc-shaped region that is typical of medium-to-strong localised interactions.33,46 This result corroborates and supports the previous conclusion drawn from the QTAIM analysis.


image file: c9ra05991a-f7.tif
Fig. 7 NCI isosurface of the toluene molecule adsorbed in InOF-1 drawn at 0.03 a.u. The main intermolecular interactions are designated. This figure was created with the VMD program.43 Some examples of these non-conventional hydrogen bonds can be found in ref. 53.

The influence of the functionalisation of InOF-1 with toluene in the CO2 capture can be rationalised in two ways: a “bottleneck”17,24,25,28 effect, and simultaneous toluene⋯CO2 and InOF-1⋯CO2 interactions. The former implies a reduction in the pore size, caused by the presence of the adsorbed toluene molecules, that forces the CO2 molecules to slow down, enhancing in this way its adsorption. Electron density isosurfaces (ρ = 0.0003 a.u.) of the pristine and toluene-functionalised InOF-1, which represent the void channels of these systems,47 are depicted in Fig. 8. For our model, where there is one toluene molecule adsorbed in one pore per unit cell (there are in total two pores in the unit cell), the void volume of the corresponding pore is reduced by 19%. This value is 5% larger than previously reported for InOF-1 functionalized with 2-propanol,27 and it is plausibly one of the reasons why the CO2 uptake is larger for the toluene-functionalized InOF-1.


image file: c9ra05991a-f8.tif
Fig. 8 Electron density isosurfaces (ρ = 0.0003 a.u.), denoting the void channels of the pristine (left) and toluene-functionalized InOF-1 (right). This figure was created with VMD.43

On the other hand, it has been demonstrated that CO2 can interact with hydrocarbon aromatic rings,48–51 forming complexes where the ring plane and the plane containing the three CO2 atoms are nearly parallel. Dispersion forces and attractive electrostatic interactions between the negative π cloud of the aromatic ring and the positive region around the carbon atom of CO2 have been held as the guiding causes for this geometric disposition.48,50 In Fig. 9, the optimised structure of CO2 interacting with the adsorbed toluene molecule is depicted. As expected, the host molecule lies over the toluene ring, with an intermolecular separation of 3.120 Å. It is interesting to note that in this geometric arrangement CO2 also interacts with one aromatic ring of the biphenyl structure of InOF-1 at a slightly larger intermolecular distance of 3.294 Å (Fig. 9). Thus, there is a synergic effect between toluene and InOF-1 that also contributes to increase the CO2 capture.


image file: c9ra05991a-f9.tif
Fig. 9 Close up (left) and pore channel (right) views of CO2 captured by toluene-functionalized InOF-1. Toluene and CO2 molecules are depicted in blue and yellow, respectively. CO2⋯toluene and CO2⋯InOF-1 intermolecular distances are depicted in green (Å). This figure was created with Mercury.40,41

DRIFT spectroscopy

In order to deeply understand the interactions between toluene-functionalised InOF-1 (toluene@InOF-1) and CO2, and to provide experimental support for the interactions proposed from the computational simulations, DRIFTs in situ experiments were carried out. Fig. 10 shows the spectra of InOF-1 (as a reference), toluene@InOF-1 and the CO2 capture at different times. The presence of the bands at 3023, 2913, 2871 and 2730 cm−1 (characteristic of the C–H stretching vibrations of the aromatic ring and methyl group for toluene) observed for toluene@InOF-1 (red spectrum) and absence of these on the activated InOF-1 (black spectrum), corroborates the adsorption of toluene inside the pores of InOF-1. In addition, a peak at 3491 cm−1 can be associated to the H⋯H interaction predicted by the computational studies since, as we showed in a previous work,52 strong interactions with the μ2-OH group of InOF-1 lead to large displacements of more than 200 cm−1. Thus, when CO2 is captured, the band at 3491 cm−1 is shifted to lower energies (3502 cm−1), corroborating the interaction of CO2 with toluene. Additionally, the CO2 region of the DRIFTs spectra is observed in Fig. 11. A vibration band centred at 2335 cm−1 is observed. This band is characteristic of the asymmetric stretching modes of the CO2 molecule and increases as a function of time. As was previously described, this band does not change significatively, even with strong hydrogen bond formation.52 The band at 2323 cm−1 can be assigned to the dipole–dipole coupling between adsorbed CO2 molecules.52 Finally, peaks observed at 2343, 2353, 2357 and 2382 cm−1 (see Fig. 11) were assigned to the interactions between CO2 and the aromatic rings of toluene and InOF-1, which were suggested by the computational studies. We are know corroborating these findings in studies with other small aromatic systems, such as benzene, and its effect on the adsorption of other substances like SO2, which will be published in future works.
image file: c9ra05991a-f10.tif
Fig. 10 DRIFTs spectra collected at different CO2 adsorption times over toluene-functionalized InOF-1 at 30 °C, in the region between 3600 and 2600 cm−1.

image file: c9ra05991a-f11.tif
Fig. 11 DRIFTs spectra collected at different CO2 adsorption times over toluene-functionalized InOF-1 at 30 °C, in the region between 2400 and 2250 cm−1.

These computational analyses and DRIFTs experiments provided us a better understanding on the confinement of small amounts of toluene within InOF-1 (intermolecular interactions), and evidenced a partial obstruction of the pores (similar to other polar molecules like H2O, EtOH, MeOH and DMF) which provided a “bottleneck effect” and a synergic effect between toluene and InOF-1, as we previously reported,17,24,25,28 to enhance the CO2 capture in InOF-1.

Conclusions

The adsorption properties of toluene in InOF-1 were investigated for the first time, to the best of our knowledge. Rapid adsorption of toluene and hysteresis at 298 and 308 K demonstrated a high affinity towards InOF-1. The affinity of toluene in InOF-1 was quantified experimentally by evaluating the isosteric heat of adsorption (ΔHads = −46.81 kJ mol−1). The isothermal CO2 dynamic-capture experiments on toluene@InOF-1 demonstrated a CO2 capture of 7.28 wt%, which corresponds to an improvement of 1.38 times compared to fully activated InOF-1.

Theoretical results indicate that the toluene molecule is adsorbed through non-localised π–π interactions formed between the toluene molecule and the aromatic ring of InOF-1, which have mainly a dispersive origin, although electrostatic effects control the orientation. Moreover, some specific interactions also contribute to the adsorption process, which are weak C–H⋯O hydrogen bonds and, notably, the H⋯H contact between one hydrogen atom of the aromatic ring of toluene and the μ2-OH functional group of InOF-1, which were corroborated by DRIFTs in situ experiments. This last result indicates that this functional group of InOF-1 can participate not only in the adsorption process of polar molecules capable of forming hydrogen bonds, but also can take part in the surface assimilation of non-polar molecules such as toluene. This final finding provided the explanation to the experimental CO2 capture enhancement (toluene@InOF-1) by the creation of a “bottleneck effect” within InOF-1 and a synergic interaction between the aromatic ring of toluene with the aromatic ligands of InOF-1 and CO2.

Conflicts of interest

There are no conflicts to declare.

Acknowledgements

The authors thank Dr A. Tejeda-Cruz (powder X-ray; IIM-UNAM), CONACyT (1789), PAPIIT UNAM (IN101517), México for financial support. E. G-Z. thanks CONACyT (236879), México for financial support. Thanks to U. Winnberg (ITAM) for scientific discussions. B. L.-R. thanks UAM for a postdoctoral fellowship. We thank to the Laboratorio de Supercómputo y Visualización en Paralelo at the Universidad Autónoma Metropolitana (UAM) Iztapalapa for access to their computer facilities. H. A. L.-G. thanks Antonio Gómez-Cortés for technical assistance.

Notes and references

  1. J. T. Litynski, S. M. Klara, H. G. McIlvried and R. D. Srivastava, Environ. Int., 2006, 32, 128–144 CrossRef CAS.
  2. International Energy Agency, CO2 Emissions, https://www.iea.org/statistics/co2emissions/, accessed 5 May 2019 Search PubMed.
  3. W. Y. Cheah, P. L. Show, J. S. Chang, T. C. Ling and J. C. Juan, Bioresour. Technol., 2015, 184, 190–201 CrossRef CAS.
  4. J. Gibbins and H. Chalmers, Energy Policy, 2008, 36, 4317–4322 CrossRef.
  5. IUPAC, Materials for CO2 Capture, https://iupac.org/materialschemistryedu/environmental/materials-for-co2-capture/, accessed 5 May 2019 Search PubMed.
  6. J. G. J. Olivier, G. Janssens-Maenhout, M. Muntean and J. A. H. W. Peters, Trends in global CO2 emissions: 2015 report, 2015 Search PubMed.
  7. M. Poliakoff, W. Leitner and E. S. Streng, Faraday Discuss., 2015, 183, 9 RSC.
  8. K.-H. Kim, S. A. Jahan and E. Kabir, Environ. Int., 2013, 59, 41–52 CrossRef CAS.
  9. P. Kumar, K. H. Kim, E. E. Kwon and J. E. Szulejko, J. Mater. Chem. A, 2015, 4, 345–361 RSC.
  10. K. Vellingiri, P. Kumar, A. Deep and K. H. Kim, Chem. Eng. J., 2017, 307, 1116–1126 CrossRef CAS.
  11. S. Miachon, V. V. Syakaev, A. Rakhmatullin, M. Pera-Titus, S. Caldarelli and J. A. Dalmon, ChemPhysChem, 2008, 9, 78–82 CrossRef CAS.
  12. L. N. Ho, S. Clauzier, Y. Schuurman, D. Farrusseng and B. Coasne, J. Phys. Chem. Lett., 2013, 4, 2274–2278 CrossRef CAS.
  13. V. Rakotovao, R. Ammar, S. Miachon and M. Pera-Titus, Chem. Phys. Lett., 2010, 485, 299–303 CrossRef CAS.
  14. A. Luzar and D. Bratko, J. Phys. Chem. B, 2005, 109, 22545–22552 CrossRef CAS.
  15. D. Bratko and A. Luzar, Langmuir, 2008, 24, 1247–1253 CrossRef CAS.
  16. M. Pera-Titus, R. El-Chahal, V. Rakotovao, C. Daniel, S. Miachon and J. A. Dalmon, ChemPhysChem, 2009, 10, 2082–2089 CrossRef CAS.
  17. E. González-Zamora and I. A. Ibarra, Mater. Chem. Front., 2017, 1, 1471–1484 RSC.
  18. R. A. Peralta, B. Alcántar-Vázquez, M. Sánchez-Serratos, E. González-Zamora and I. A. Ibarra, Inorg. Chem. Front., 2015, 2, 898–903 RSC.
  19. M. R. Gonzalez, J. H. González-Estefan, H. A. Lara-García, P. Sánchez-Camacho, E. I. Basaldella, H. Pfeiffer and I. A. Ibarra, New J. Chem., 2015, 39, 2400–2403 RSC.
  20. M. Sagastuy-Breña, P. G. M. Mileo, E. Sánchez-González, J. E. Reynolds, T. Jurado-Vázquez, J. Balmaseda, E. González-Zamora, S. Devautour-Vinot, S. M. Humphrey, G. Maurin and I. A. Ibarra, Dalton Trans., 2018, 47, 15827–15834 RSC.
  21. C. T. He, J. Y. Tian, S. Y. Liu, G. Ouyang, J. P. Zhang and X. M. Chen, Chem. Sci., 2013, 4, 351–356 RSC.
  22. K. Yang, Q. Sun, F. Xue and D. Lin, J. Hazard. Mater., 2011, 195, 124–131 CrossRef CAS.
  23. J. Qian, F. Jiang, D. Yuan, M. Wu, S. Zhang, L. Zhang and M. Hong, Chem. Commun., 2012, 48, 9696–9698 RSC.
  24. E. Sánchez-González, P. G. M. Mileo, J. R. Álvarez, E. González-Zamora, G. Maurin and I. A. Ibarra, Dalton Trans., 2017, 46, 15208–15215 RSC.
  25. E. González-Zamora, J. A. Zárate, J. Balmaseda, V. Jancik, J. R. Álvarez, I. A. Ibarra, A. Campos-Reales-Pineda, D. Martínez-Otero, A. Martínez, R. A. Peralta and H. Pfeiffer, Chem. Commun., 2016, 52, 10273–10276 RSC.
  26. J. R. Álvarez, P. G. M. Mileo, E. Sánchez-González, J. Antonio Zárate, J. Rodríguez-Hernández, E. González-Zamora, G. Maurin and I. A. Ibarra, J. Phys. Chem. C, 2018, 122, 5566–5577 CrossRef.
  27. J. E. Sánchez-Bautista, B. Landeros-Rivera, T. Jurado-Vázquez, A. Martínez, E. González-zamora, J. Balmaseda, R. Vargas and I. A. Ibarra, Dalton Trans., 2019, 48, 5176–5182 RSC.
  28. E. Sánchez-González, E. González-Zamora, D. Martínez-Otero, V. Jancik and I. A. Ibarra, Inorg. Chem., 2017, 56, 5863–5872 CrossRef.
  29. B. Civalleri, C. M. Zicovich-Wilson, L. Valenzano and P. Ugliengo, CrystEngComm, 2008, 10, 405–410 RSC.
  30. M. F. Peintinger, D. Vilela Oliveira and T. Bredow, J. Comput. Chem., 2013, 34, 451–459 CrossRef CAS.
  31. R. Dovesi, R. Orlando, A. Erba, C. M. Zicovich-Wilson, B. Civalleri, S. Casassa, L. Maschio, M. Ferrabone, M. D. La Pierre, P. D'Arco, Y. Noël, M. Causà, M. Rérat and B. Kirtman, Int. J. Quantum Chem., 2014, 114, 1287–1317 CrossRef CAS.
  32. R. F. W. Bader, Atoms in molecules: a quantum theory, Oxford University Press, Oxford, 1990 Search PubMed.
  33. E. R. Johnson, S. Keinan, P. Mori-Sánchez, J. Contreras-García, A. J. Cohen and W. Yang, J. Am. Chem. Soc., 2010, 132, 6498–6506 CrossRef CAS.
  34. R. Hernández-Esparza, S. M. Mejía-Chica, A. Zapata-Escobar, A. Guevara-García, A. Martínez-Melchor, J. Hernández-Pérez, R. Vargas and J. Garza, Comput. Chem., 2014, 35, 2272–2278 CrossRef.
  35. J. Contreras-García, E. R. Johnson, S. Keinan, R. Chaudret, J. P. Piquemal, D. N. Beratan and W. Yang, J. Chem. Theory Comput., 2011, 7, 625–632 CrossRef.
  36. D. Ma, Y. Li and Z. Li, Chem. Commun., 2011, 47, 7377–7379 RSC.
  37. O. Bludský, M. Rubeš, P. Soldán and P. Nachtigall, J. Chem. Phys., 2008, 128, 114102 CrossRef.
  38. R. Kruszynski and T. Sierański, Cryst. Growth Des., 2016, 16, 587–595 CrossRef CAS.
  39. R. Podeszwa, R. Bukowski and K. Szalewicz, J. Phys. Chem. A, 2006, 110, 10345–10354 CrossRef CAS.
  40. C. F. Macrae, P. R. Edgington, P. McCabe, E. Pidcock, G. P. Shields, R. Taylor, M. Towler and J. van de Streek, J. Appl. Crystallogr., 2006, 39, 453–457 CrossRef CAS.
  41. C. F. Macrae, I. J. Bruno, J. A. Chisholm, P. R. Edgington, P. McCabe, E. Pidcock, L. Rodriguez-Monge, R. Taylor, J. van de Streek and P. A. Wood, J. Appl. Crystallogr., 2008, 41, 466–470 CrossRef CAS.
  42. P. Hobza, H. L. Selzle and E. W. Schlag, J. Phys. Chem., 1996, 100, 18790–18794 CrossRef CAS.
  43. W. Humphrey, A. Dalke and K. Schulten, J. Mol. Graphics, 1994, 14, 33–38 CrossRef.
  44. C. F. Matta, J. Hernández-Trujillo, T. H. Tang and R. F. Bader, Chem.–Eur. J., 2003, 9, 1940–1951 CrossRef CAS.
  45. J. D. Dunitz and A. Gavezzotti, Angew. Chem., Int. Ed., 2005, 44, 1766–1787 CrossRef CAS.
  46. G. Saleh, C. Gatti, L. Lo Presti and J. Contreras-García, Chem.–Eur. J., 2012, 18, 15523–15536 CrossRef CAS.
  47. M. J. Turner, J. J. McKinnon, D. Jayatilaka and M. A. Spackman, CrystEngComm, 2011, 13, 1804–1813 RSC.
  48. J. W. Shen, K. B. Domański, O. Kitao and K. Nakanishi, Fluid Phase Equilib., 1995, 104, 375–390 CrossRef CAS.
  49. M. Besnard, M. I. Cabaço, D. Talaga and Y. Danten, J. Chem. Phys., 2008, 129, 224511 CrossRef CAS.
  50. L. Chen, F. Cao and H. Sun, Int. J. Quantum Chem., 2013, 113, 2261–2266 CrossRef CAS.
  51. J. Witte, J. B. Neaton and M. Head-Gordon, J. Chem. Phys., 2014, 140, 104707 CrossRef.
  52. H. A. Lara-García, B. Landeros-Rivera, E. González-Zamora, J. Aguilar-Pliego, A. Gómez-Cortés, A. Martínez, R. Vargas, G. Diaz and I. A. Ibarra, Dalton Trans., 2019, 48, 8611–8616 RSC.
  53. (a) C. F. Matta, Hydrogen–Hydrogen Bonding: The Non-Electrostatic Limit of Closed-Shell Interaction Between Two Hydrogen atoms. A Critical Review, in Hydrogen Bonding-New Insights, ed. S. J. Grabowski, Springer, Netherlands, Dordrecht, 2006, pp. 337–375 Search PubMed; (b) A. Paul, M. Kubicki, C. Jelsch, P. Durand and C. Lecomte, Acta Crystallogr., Sect. B: Struct. Sci., Cryst. Eng. Mater., 2011, 67, 365–378 CrossRef CAS; (c) V. R. Hathwar, M. Sist, M. R. V. Jørgensen, A. H. Mamakhel, X. Wang, C. M. Hoffmann, K. Sugimoto, J. Overgaard and B. B. Iversen, IUCrJ, 2015, 2, 563–574 CrossRef CAS.

Footnote

Electronic supplementary information (ESI) available: PXRD data, derivation of the isosteric enthalpy of adsorption for toluene and theoretical calculations. See DOI: 10.1039/c9ra05991a

This journal is © The Royal Society of Chemistry 2019