Nearly one-third of the global population lives in arid areas with limited access to clean water.1 Therefore, innovative solutions are urgently wanted to address this global water crisis affecting millions of people. Atmospheric water accounts for 1018 cubic meters, that constitutes 3% of the total fresh water accessible on our planet.2 Present everywhere and anytime, this water, once harvested, could help to ease the global water crisis.3
Metal-organic frameworks (MOFs) have emerged as promising materials for atmospheric water capture.4,5 Several MOFs have been shown to exhibit three major characteristics for this purpose: 1) high water stability, 2) steep water uptake step at low relative humidity (RH) (<40%) and 3) low regeneration energy for recycling purposes. Importantly, unlike other porous materials,6 MOFs demonstrate a high potential for tunability of surface area, pore volume, and pore structure via modifications at the molecular level. MOFs demonstrate a high potential for tunability of surface area, pore volume, and pore structure via modifications at the molecular level, which directly influences their water sorption properties Enhancement of water uptake at low RH while retaining all the above-mentioned characteristics has been a long-standing problem in the research on water-harvesting MOFs.
In addition to MOFs a diverse range of materials such as silica gel, porous polymers, and zeolites have been tested for their water sorption properties.10 However, all of them suffer from drawbacks that prevent their usage in water-harvesting devices. Thus, zeolites, although showing a steep water uptake at low pH, require enormous amounts of energy for regeneration. Otherwise, they experience structure poisoning through permanent water enclosure in their pores that negatively impacts their efficacy. The water sorption isotherm profiles of silica gel and porous polymers lack steepness that results in a low working capacity of these materials.
Among MOFs, only a few examples have been shown to demonstrate the desirable properties for water-harvesting applications.11 The moisture sensitivity and hydrophobicity of most MOF structures is an ongoing problem,12 therefore novel structures are highly wanted.
Herein, we report a novel water-stable MOF with higher water uptake at low RH compared to its previous analogs.7,8,9 In this disclosure, we introduce a linker extension/functionalization strategy to obtain MOFs structures with boosted water uptake capacities. The extension of the linkers, wherein at least one of m or n is 1-5, provide MOFs with enhanced pores sizes and volumes. Moreover, further customization of extended linkers by changing their heterocyclic core (X, Y, Z, I) or via introduction of substituents (R1-R5) can be used to adjust or tune the water sorption properties of the respective MOFs.
The disclosed linker extension/functionalization strategy can be used increase the water uptake of the existing MOFs without significant negative effects on their longevity and hydrophilicity.
The targeted purpose of the described linker extension/functionalization strategy is to increase the water uptake of MOFs for deployment in water-harvesting devices. This application allows for usage of less material to capture the same amount of moisture at the desired RH as compared to the previously utilized MOFs.
Furthermore, the additional modifications of the extended linkers provide a variety of MOF structures with diverse water-harvesting properties. Thus, in addition to water-harvesting devices, dehumidifiers, heat pumps, adsorption refrigerators, and other appliances can benefit from usage of these novel MOF structures.
In an aspect the invention provides novel water-stable metal-organic framework (MOF) compositions with linker extension/functionalization provide higher water uptake at low relative humidity
In an aspect the invention provides a metal-organic framework (MOF) composition, comprising a metal complexed with linkers of formula:
In an aspect the invention provides a metal-organic framework (MOF), comprising repeating cores, wherein the cores comprise secondary building units connected to organic ligands (linkers), wherein the secondary building units comprise one or more metals or metal-containing complexes, wherein the organic ligands (linkers) are of formula I (supra), and wherein the secondary building units are connected to the organic ligands through the oxygen atoms of the carboxylate groups in the organic ligands (linkers).
In embodiments:
In embodiments the MOF composition comprises linkers of formula II:
In an aspect the invention provides a MOF or composition herein, wherein the linkers comprise a formula of Table 1, 2, 3 or 4.
In embodiments, a MOF or composition herein, wherein the metal is a metal ion selected from Li+, Na+, K+, Rb+, Cs+, Be2+, Mg2+, Ca2+, Sr2+, Ba2+, Sc3+, Sc2+, Sc+, Y3+, Y2+, Y+, Ti4+, Ti3+, Ti2+, Zr4+, Zr3+, Zr2+, Hf4+, Hf3+, V5+, V4+, V3+, V2+, Nb5+, Nb4+, Nb3+, Nb2+, Ta5+, Ta4+, Ta3+, Ta2+, Cr6+, Cr5+, Cr4+, Cr3+, Cr2+, Cr+, Cr, Mo6+, Mo5+, Mo4+, Mo3+, Mo2+, Mo+, Mo, W6+, W5+, W4+, W3+, W2+, W+, W, Mn7+, Mn6+, Mn5+, Mn4+, Mn3+, Mn2+, Mn+, Re7+, Re6+, Re5+, Re4+, Re3+, Re2+, Re+, Re, Fe6+, Fe4+, Fe3+, Fe2+, Fe+, Fe, Ru8+, Ru7+, Ru6+, Ru4+, Ru3+, Ru2+, Os8+, Os7+, Os6+, Os5+, Os4+, Os3+, Os2+, Os+, Os, Co5+, Co4+, Co3+, Co2+, Co+, Rh6+, Rh5+, Rh4+, Rh3+, Rh2+, Rh+, Ir6+, Ir5+, Ir4+, Ir3+, Ir2+, Ir+, Ir, Ni3+, Ni2+, Ni+, Ni, Pd6+, Pd4+, Pd2+, Pd+, Pd, Pt6+, Pt5+, Pt4+, Pt3+, Pt2+, Pt+, Cu4+, Cu3+, Cu2+, Cu+, Ag3+, Ag2+, Ag+, Au5+, Au4+, Au3+, Au2+, Au+, Zn2+, Zn+, Zn, Cd2+, Cd+, Hg4+, Hg2+, Hg+, B3+, B2+, B+, Al3+, Al2+, Al+, Ga3+, Ga2+, Ga+, In3+, In2+, In1+, Tl3+, Tl+, Si4+, Si3+, Si2+, Si+, Ge4+, Ge3+, Ge2+, Ge+, Ge, Sn4+, Sn2+, Pb4+, Pb2+, As5+, As3+, As2+, As+, Sb5+, Sb3+, Bi5+, Bi3+, Te6+, Te5+, Te4+, Te2+, La3+, La2+, Ce4+, Ce3+, Ce2+, Pr4+, Pr3+, Pr2+, Nd3+, Nd2+, Sm3+, Sm2+, Eu3+, Eu2+, Gd3+, Gd2+, Gd+, Tb4+, Tb3+, Tb2+, Tb+, Db3+, Db2+, Ho3+, Er3+, Tm4+, Tm3+, Tm2+, Yb3+, Yb2+, Lu3+, and combinations thereof, including any complexes which contain the metals or metal ions listed above, as well as any corresponding metal salt counter-anions.
In embodiments, the invention provides a MOF or composition herein, wherein the metal is selected from aluminum, titanium, zirconium, and hafnium.
In an aspect, the invention provides a method of making a MOF or composition herein, comprising complexing the metal with the linkers to form the MOF composition.
In an aspect, the invention provides a MOF or composition herein, comprising absorbing water in the composition.
The invention encompasses all combinations of the particular embodiments recited herein, as if each combination bad been laboriously recited.
Unless contraindicated or noted otherwise, in these descriptions and throughout this specification, the terms “a” and “an” mean one or more, the term “or” means and/or It is understood that the examples and embodiments described herein are for illustrative purposes only and that various modifications or changes in light thereof will be suggested to persons skilled in the art and are to be included within the spirit and purview of this application and scope of the appended claims. All publications, patents, and patent applications cited herein, including citations therein, are hereby incorporated by reference in their entirety for all purposes.
Linker L1, an extended version of 1H-3,5-pyrazole dicarboxylic acid (linker of MOF-303), was synthesized via a two-step procedure employing a Wittig reaction followed by hydrolysis. MOF-LA2 was obtained via solvothermal synthesis between an aluminum salt, AlCl3·6H2O, and linker (L1) either in aq. NaOH solution or DMF/H2O mixtures.
MOF-LA2 adopts an isoreticular structure to MOF-303, as shown by its powder X-ray diffraction pattern (PXRD). The water sorption isotherm profile reveals a steep step at 26% RH with overall water uptake capacity of 0.63 g/g. This is almost 1.5 higher than that of MOF-303. Although shifted to the right in comparison with MOF-303, the water uptake step of MOF-LA2 is still in the region of RH values corresponding to the conditions at the most arid places in the world.
The cycling experiment shows negligible decrease in the total water uptake of MOF-LA2 after 29 additional cycles.
Several linker embodiments with different substituents R for the MOF-LA2 family are shown in Table 1. Introducing hydrophilic groups such as —OH and —NH2 will shift the isotherm to even more arid RH values, while introducing hydrophobic/neutral groups such as CH3 or halogens will move the isotherm to higher RHs. Further linker embodiments with variations of the core (X, Y, Z, l) are represented in Table 2.
All of these can be synthesized using an identical approach as that for L1. Analogously to MOF-LA2, the tentative MOFs can be obtained via solvothermal synthesis either in aq. NaOH solution or DMA/H2O mixtures. Linkers L1-L3 (linker type I), with a very similar angle between the carboxylic groups as L1) (˜160°), produce isoreticular MOFs to MOF-303 exhibiting cis-trans-shared AlO6 chain inorganic building units (also called secondary building units, SBUs;
Embodiments of longer versions of L1-L9 linkers that yield the MOF-LA4 family are represented in Table 3. Representative examples of novel linkers for the MOF-LA5 family (n,m-variations) are shown in Table 4.
A representative method for synthesis of the linkers L10-L18, shown for L15, relies on a Knovenagel condensation of the corresponding bis-aldehyde with malonic acid13.
ABSTRACT: A linker extension strategy for generating metal-organic frameworks (MOFs) with a superior moisture-capturing properties is presented. Applying a cooperative design approach that combines experiment and computation results in MOF-LA2-1 {[Al(OH)(PZVDC)], where PZVDC2− is (E)-5-(2-carboxylatovinyl)-1H-pyrazole-3-carboxylate} exhibiting a 50% water capacity increase compared to the state-of-the-art water-harvesting material MOF-303. The power of this approach is the increase in pore volume without compromising the ability of the MOF to harvesting water in and environments under long-term uptake and release cycling, as well as affording a reduction in regeneration heat and temperature. Density functional theory calculations and Monte Carlo simulations give detailed insight pertaining to framework structure, water interactions within its pores, and the resulting water sorption isotherm.
Water stress already affects about half of the world population.1,2 Given that there is clean water in the atmosphere, porous and hygroscopic sorbents are being investigated for water extraction from air.3,4 An ideal water-harvesting material should (i) take up water at a desirable relative humidity (RH), including from desert air, (ii) exhibit step-shaped moisture uptake behavior to allow for uptake and release of large amounts of water by minor perturbations in temperature or pressure, (iii) display facile water release to reduce the energy consumption and increase the productivity. (iv) have hydrothermal stability to enable long-term operation, and (v) be made from non-toxic, abundant components using environmentally benign processes.
In this regard, metal-organic frameworks (MOFs) are promising materials because of the facility with which they can be designed and modified to achieve a desired property,5-7 which has led to their successful implementation for atmospheric water harvesting.8-14 In particular, the discovery of MOF-303 {[Al(OH)(PZDC)], where PZDC2− is 1H-pyrazole-3,5-dicarboxylate;
The conundrum solved by the present study is how to retain the alternating hydrophilic-hydrophobic pocket environment while simultaneously increasing the water uptake capacity of the framework. In other words, how to increase the pore volume of MOF-303 without compromising its favorable water-uptake attributes. The usual strategy to increase the pore volume of aluminum MOFs made from rodlike SBUs is linker extension, involving either polycyclic aromatic linkers or appending additional aromatic rings to the linker.16-19 However, these approaches generated either hydrophobic, less porous, or large-pore hydrolytically labile aluminum frameworks.16,19,22
Herein, through an integrated experimental computational approach we identified and implemented a suitable linker extension strategy involving appending a single vinyl group to PZDC2− (
At the outset of this study, we hypothesized that addition of a relatively compact, yet long group to the hydrophilic H2PZDC linker utilized in MOF-303 will enhance its water uptake capacity while leveraging its hydrophilic nature and its excellent stability (
The resulting microcrystalline powder was first characterized by powder X-ray diffraction (PXRD) analysis. A significant 2θ shift of the corresponding PXRD reflections to lower values compared to MOF-303 was indicative of successful isoreticular extension of the parent framework (
Thus, we utilized periodic DFT optimizations to probe the relative stability of the different possible linker configurations in the MOF-LA2-1 structure at the unit cell parameters extracted from SCXRD data (Section S3.2). In this context, a total of 16 possible backbone configurations of the framework featuring different positions and orientations of the pyrazole and vinyl groups in the hydrophilic cavity of the MOF were considered. Generally, the configurations where the pyrazole functionalities were on the same side of the pocket (ZUS, from German ‘zusammen’, together; as in
As discussed earlier, MOF-LA2-1 was derived from MOF-303 by adding a vinyl group to the H2PZDC linker molecule with the goal of enhancing its water uptake capacity while retaining the arrangement of the pyrazole functionalities, which were determined to be key to the water-harvesting properties of MOF-303. Having determined the most stable framework configuration, we investigated the primary water adsorption sites of MOF-LA2-1 in this arrangement computationally and compared them with the respective sites in MOF-303 (
Considering the insights gained through DFT calculations, we refined the structural model of MOF-LA2-1 in its most stable configuration (
Next, the thermal stability and porosity of MOF-LA2-1 were studied using thermogravimetric analysis (TGA) and nitrogen sorption analysis, respectively. TGA under both argon and air atmosphere revealed no significant weight loss below 300° C. This indicated excellent stability required for thermal regeneration during the water-harvesting operation. Initial evaluation of the nitrogen sorption isotherm at 77 K of MOF-LA2-1 revealed a Brunauer-Emmett-Teller (BET) surface area and a pore volume of 1892 m2 g−1 and 0.67 cm3 g−1, respectively—values 1.4 times higher compared to MOF-303.15
The water-harvesting properties of MOF-LA2-1 were first probed by performing water sorption measurements under isothermal conditions. Similar to the parent framework, the extended framework displayed a pre-step in its isotherm, which is very likely associated with the presence of a hydrophilic pocket formed by the pyrazole functionalities, thus forming strong water adsorption sites, as was previously observed for MOF-303.15 Notably, the water sorption isotherm profile exhibited a steep step at 26% RH with a total water uptake of 0.64 g g−1—a 50% higher water capacity than MOF-303 (
Furthermore, the regeneration temperature of MOF-LA2-1 was probed by measuring isobaric desorption curves. These measurements were conducted at water vapor pressures of 1.27 and 1.70 kPa (corresponding to 30 and 40% RH at 30° C., respectively) and demonstrated substantially reduced water release temperatures compared to MOF-303 (
To examine the stability of MOF-LA2-1 at the operational conditions, temperature swing adsorption-desorption cycling was performed at 1.70 kPa water vapor pressure (
We next studied the dependence of the water adsorption behavior on the different linker configurations of MOF-LA2-1. For that, force-field-based Monte Carlo simulations in the Gibbs ensemble were used to compute the water adsorption isotherms at 298 K (Section S3.4). We focused these efforts on the most stable ZUS and ENT configurations, which served as representative examples of the different structural ensembles (Section S3.4). The simulated water sorption isotherms of the two structural types displayed significantly different profiles (
In conclusion, we have demonstrated a linker ‘arm’ extension strategy and employed it to significantly enhance the water-harvesting properties of the state-of-the-art water-harvesting material MOF-303. Importantly, this features a 50% increase of the water uptake capacity as well as reduced operational energetic requirements, while retaining the ability for moisture capture in arid regions and the hydrothermal stability suitable for long-term uptake and release cycling. This approach is generalizable and is particularly useful for commercially relevant aluminum-based MOFs.
Synthesis of (E)-5-(2-carboxyvinyl)-1H-pyrazole-3-carboxylic acid (H2PZVDC):
Step 1:13 A 100-mL round-bottom flask equipped with a stirring bar was charged with 1 (1.5 g, 8.9 mmol. 1 equiv.) and dry THF (50 mL) under argon atmosphere. The mixture was cooled down to −10° C. using acetone/ice bath, and 2 (3.5 g, 10.5 mmol, 1.2 equiv.) was added portion-wise. The reaction was allowed to warm up to room temperature overnight. After concentrating the resulting solution under reduced pressure, a mixture containing E and Z-isomers was identified via 1H NMR analysis. The desired E-isomer 3 was isolated via column chromatography using acetone/hexane (5/1) as eluent (Rf=0.1). Yield: 1.3 g, 65%
1H NMR (400 MHz, CDCl3) δ 10.93 (s, 1H), 7.67 (d, J=16.0 Hz, 1H), 7.04 (s, 1H), 6.48 (d, J=16.0 Hz, 1H), 4.41 (q, J=7.1 Hz, 2H), 3.81 (s, 3H), 1.41 (t, J=7.1 Hz, 3H) ppm.
Step 2: A 100-mL round-bottom flask equipped with a stirring bar was charged with 3 (1.3 g, 5.8 mmol, 1 equiv.), MeOH (50 mL) and aqueous NaOH solution (20 mL, 1.5 M, 5 equiv.). The reaction was heated at 50° C. (oil bath temperature) until the starting material was consumed, as monitored by TLC (2 h). The solution was concentrated under reduced pressure and 5 M HCl was added dropwise until pH=2-3. The resulting precipitate was filtered off and thoroughly washed with H2O (4×10 mL) and MeOH (1×5 mL) After drying at 50° C. in vacuo, the linker H2PZVDC was obtained as white powder. Yield: 1.0 g, 95%. 1 H NMR (500 MHz, DMSO-d6) δ 13.80-13.10 (br. s, 3H), 7.46 (d, J=16.2 Hz, 1H), 7.17 (s, 1H), 6.53 (d, J=16.1 Hz, 1H). 13C NMR (126 MHz, DMSO-d6) ppm. δ 167.4, 161.4, 120.6, 108.4 ppm. HRMS (m/z). [M−H]− calcd. for C7H5N2O4, 181.0255; found, 181.0255.
In a 4-mL scintillation vial, linker H2PZVDC (91.0 mg, 0.5 mmol, 1 equiv.) was dissolved in N,N-dimethylformamide (DMF) (0.6 mL) upon sonication. An aqueous solution of AlCl3 6H2O) (2.4 mL, 0.2 M, 1 equiv.) was added dropwise, and the resulting mixture was heated in a 120°° C. oven for 24 h. After cooling down to room temperature, the white precipitate was collected by centrifuging and washed with H2O (3×30 mL) and MeOH (3×30 mL). MOF-LA2-1 was activated under dynamic vacuum (˜10−3 mbar) for 12 h at room temperature, followed by gradual heating to 120°° C. for 6.5 hours. Yield. 65.0 mg. 58%. Elem. Anal. of MOF-LA2-1. Calcd. for C56H40N16O40Al8. C, 37.52; H, 2.25, N, 12.50%. Found: C, 36.78; H, 2.38, N, 11.95%.
In a 50-mL round-bottom flask, linker H2PZVDC (364 mg, 2 mmol, 1 equiv.) and NaOH (160 mg, 4 mmol, 2 equiv) were dissolved in deionized water (10 mL) upon sonication. An aqueous solution of AlCl3·6H2O (6 mL, 0.33 M, 1 equiv.) was added dropwise for 10 minutes, and the reaction mixture was heated to 120°° C. and refluxed for 2 hours. After cooling down to room temperature, the white powder was collected by centrifuging and washed with deionized water (2×10 mL) and EtOH (3×10 mL). The white powder was dried under air overnight, followed by activation under dynamic vacuum (˜10−3 mbar) for 12 hours at 120° C. Yield: 301 mg. 66%. Elem. Anal. of MOF-LA2-1: Calcd. for C56H40N16O40Al8: C, 37.52; H, 2.25; N, 12.50%. Found: C. 37.29, H, 2.43; N. 12.10%.
We first constructed a hypothetical MOF, MOF-LA2-1, from the parent MOF-303 wherein the PZDC2− (1H-pyrazole-3,5-dicarboxylate) linkers of MOF-303 were replaced with PZVDC2− linkers containing an extension by a vinyl group. Without any a priori knowledge of the experimental crystal structure of this MOF, we constructed a DFT-optimized structure of this MOF, where the contact angle between the aluminum oxide rods and linkers was similar to that in MOF-303 with the pyrazole groups forming an alternating pattern of hydrophilic-hydrophobic pockets. In this arrangement, the vinyl group extension allowed for a more than 30% increase in pore volume compared to the parent MOF (0.598 cm3 g−1 versus 0.452 cm3 g−1). Force-field-based Monte Carlo simulations in the NpT-Gibbs ensemble (see Section S1, Computational Methods for more details) were used to predict the water adsorption isotherm of MOF-LA2-1 at 298 K. The simulated adsorption isotherm showed a steep step at a relative humidity of ˜18% and an overall water uptake of 0.6 g g−1—a 1.5-fold increase compared to the MOF-303 uptake predicted using the same procedure.
We utilized DFT calculations to probe the relative stability of the different possible linker configurations in the MOF-LA2-1 structure. A total of sixteen different linker configurations (
The relative stabilities of the different linker configurations were evaluated using periodic DFT optimizations (PBE-D3/850 eV level of theory, see Section S1, Computational Methods for more details) of the framework atoms of the empty MOF constrained to the lattice parameters determined experimentally (see Section S6 for more details). In general, the ZUS linker configurations, in which the pyrazole groups are opposite to each other in the hydrophilic cavity of the MOF, were found to be more stable compared to the ENT linker configurations, which could be attributed to potential hydrogen-bond stabilization between the opposing pyrazole groups in the ZUS linker configurations. Moreover, the ZUS linker configurations in which the pyrazole groups were present on the wider side of the hydrophilic cavity {ZUS(w)} were found to be more stable compared to the linker configurations in which the pyrazole groups were present on the narrower side of the hydrophilic pocket {ZUS(n)}. This could be explained by potential steric constraints associated with both relatively large pyrazole moieties being present on the narrow side of the pocket. In contrast to the ZUS linker configurations, in which the pyrazole groups in the hydrophilic MOF cavity were aligned in the same plane, the pyrazole groups in the hydrophilic cavity of the MOF with ENT linker configurations were not aligned in a common plane. The orientation of the vinyl group was also found to influence the relative stability of the MOF-LA2-1 structures. Generally, the presence of cis-oriented vinyl groups relative to the pyrazoles in the ZUS(w) configurations destabilized the MOF structures In contrast, the ZUS(n) configurations were stabilized by presence of cis-oriented vinyl groups.
To summarize, the ZUS(w)-trans,trans linker arrangement was found to be the most stable configuration of MOF-LA2-1. Four other linker configurations (namely ZUS(n)-cis,trans; ENT(w)-trans,cis; ZUS(w)-trans,cis; and ZUS(w)-cis,trans) were identified as energetically reachable linker configurations {with ΔE values of 27-29 kJ mol−1 per asymmetric unit [Al(OH)(PZVDC)]2, that is ˜4 kBT at MOF synthesis temperatures of 373-393 K}. The first four structures were used as representative structures to investigate the water adsorption behavior in MOF-LA2-1; calculations were not carried out for ZUS(w)-cis,trans due to its similarity to ZUS(w)-trans,cis.
MOF-LA2-1 was derived from MOF-303 by adding a compact, yet long vinyl group to the PZDC2− linker of MOF-303 with the goal of enhancing the water uptake capacity of MOF-303 while retaining its arrangement of the pyrazole functionalities, which was determined to be key for the favorable water-harvesting properties of MOF-303. To demonstrate this, we investigated the primary water adsorption sites in the ZUS(w)-trans,trans and ENT(w)-trans,cis linker configurations of MOF-LA2-1, which served as representative structures for the ZUS and ENT configurations. Indeed, similar to the primary water adsorption sites determined previously in MOF-303 (
In the ZUS(w)-trans,trans linker configuration, the first water molecule forms four H bonds (2.7-3.0 Å) with the framework—one each with the NH and N groups of the two neighboring linkers, and two with the μ2-OH groups of the aluminum oxide rod (ΔEads,avg=−84.6 kJ mol−1,
In contrast, the H2O adsorption sites differ in the ENT(I)-trans,cis linker configuration, which could be explained by the spatial separation of the pyrazole groups. The first H2O molecule adsorbs through four H bonds with the framework (2.7-2.9 Å)—one with the NH group, two with the μ2-OH groups, and one with the carboxylate group of the linker (ΔEads,avr=−77.4 kJ mol−1;
We next probed the dependence of the water adsorption behavior on the different linker configurations of MOF-LA2-1. Force-field-based Monte Carlo (MC) simulations in the isobaric-isothermal (NpT) Gibbs ensemble were used to compute the water adsorption isotherms at 298 K. Considering the similarity of the primary adsorption sites in MOF-LA2-1 and MOF-303 (Section S3.3), the simulation setup was chosen to be similar to a previous study focusing on the prediction of water adsorption isotherms of MOF-303 (see Section S1, Computational Methods for more details).2 Rigid framework structures of MOF-LA2-1, optimized in the presence of 4 H2O molecules per unit cell (corresponding to 1 H2O per asymmetric unit) that were deleted prior to the MC simulations, were used for these calculations. This arrangement led to an expanded hydrophilic cavity, thus accounting for the structural flexibility of the MOF, which was previously shown to be important for obtaining the appropriate initial water uptake in MOF-303.2
Using the above-described procedure, the water adsorption isotherms of MOF-LA2-1 in the ZUS(w)-trans,trans; ZUS(n)-cis,trans; ZUS(w)-trans,cis; and ENT(w)-trans,cis linker configurations were simulated. Noteworthy, the ZUS and ENT linker configurations exhibit significantly different water adsorption behavior. In agreement with the measured adsorption isotherm, both the ZUS(w)-trans,trans and ZUS(w)-trans,cis configurations, in which the pyrazole groups are present on the wider side of the hydrophilic cavity, show an initial water uptake of ˜5 water molecules per unit cell already at a relative humidity (RH) of 5% and a sharp step in the isotherm step at ˜30% RH, slightly shifted compared to the experimental isotherm. We note that these two linker configurations differ only in the orientation of the vinyl groups, and the similar adsorption behavior of these two linker configurations suggests that the orientation of the vinyl groups (cis or trans) does not significantly influence the overall adsorption isotherm. On the other hand, the ZUS(n)-cis,trans linker configuration, in which the pyrazole groups are present on the narrowed side of the hydrophilic cavity, does not exhibit the initial water uptake at <10% RH observed in the experimental isotherm, even though the framework structure used for this linker configuration was optimized in the presence of 4 H2O molecules per unit cell. This is consistent with the observation that the water molecules did not adsorb at the ‘strong’ adsorption sites during the DFT optimization, as observed for the other ZUS linker configurations. Instead, the adsorbed water molecules move out of the plane of the two pyrazole linkers into the MOF pore, thereby not expanding the cavity significantly upon water adsorption. This linker configuration displayed a steep step in the isotherm at ˜22% RH, thus exhibiting a larger deviation from the experimental isotherm than the ZUS(w) configurations
In contrast to the steep step observed in the adsorption isotherms for the three investigated ZUS linker configurations, the ENT(w)-trans,cis linker configuration exhibited a more gradual increase in its water uptake. The pyrazole functionalities are more distributed across the hydrophilic cavity, leading to a greater number of energetically favorable adsorption sites in the framework compared to the ZUS linker configurations. Considering the steep profile of the experimental isotherm, we conclude that the ENT linker configuration is not a suitable structural model, while the ZUS(w)-trans,trans and ZUS(w)-trans,cis linker configurations appear to be good representatives of the synthesized MOF-LA2-1.
This invention was made with government support under grant number HR0011-21-C-002 from the Department of Defense Advanced Research Projects Agency. The government has certain rights in the invention.
Number | Date | Country | |
---|---|---|---|
63480518 | Jan 2023 | US | |
63342060 | May 2022 | US |
Number | Date | Country | |
---|---|---|---|
Parent | PCT/US2023/065641 | Apr 2023 | WO |
Child | 18943182 | US |