Application of metal–organic frameworks with coordinatively unsaturated metal sites in storage and separation of methane and carbon dioxide

Natural gas has gain popularity for transportation among other fuels since it is the cleanest burning fossil fuel. However, the important challenge for utilizing natural gas is its comparatively low volumetric energy storage density. Consequently, a suitable natural gas storage is needed. Adsorbed natural gas (ANG) is an interesting alternative because it could be expected to reduce the cost and potential damage from compressed natural gas (CNG) and liquefied natural gas (LNG) technology. Comparative adsorption of methane and carbon dioxide on activated carbon ZIF-8, UiO-66, and MIL-53 (Al) was investigated at 35 ?C and up to 100 psi. The addition of PVDF in ZIF-8 and activated carbon were also studied including 75 wt% ZIF-8, 50 wt% ZIF-8, 25 wt% ZIF-8, 50 wt% ZIF-8, and 25 wt% ZIF-8. The result shows that the methane and carbon dioxide adsorption increase with the pressure. MIL-53 shows the highest methane and carbon dioxide adsorption. The high surface area and micropore volume corresponds to the high methane and carbon dioxide adsorption. However, the high micropore volume to total pore volume ratio also contributes to higher methane adsorption in the case of ZIF-8 and UiO-66. ZIF-8 has higher methane adsorption than UiO-66 although they have about the same surface area and micropore volume. On the contrary, UiO-66 has higher carbon dioxide adsorption than ZIF-8 affecting from chemical properties such as an open metal site and an organic ligand. Moreover, ZIF-8 has the highest CH4/CO2 selectively because it has high surface area, high micropore volume, high micropore volume to total pore volume ratio, and proper open metal site and organic ligand.

Open AccessCCS ChemistryRESEARCH ARTICLE3 Oct 2022Fluorous Metal–Organic Frameworks with Unique Cage-in-Cage Structures Featuring Fluorophilic Pore Surfaces for Efficient C2H2/CO2 Separation Xing-Ping Fu†, Yu-Ling Wang†, Xue-Feng Zhang, Zhenjie Zhang, Chun-Ting He and Qing-Yan Liu Xing-Ping Fu† College of Chemistry and Chemical Engineering, Key Laboratory of Functional Small Molecules for Ministry of Education, Jiangxi Normal University, Nanchang, Jiangxi 330022 Department of Ecological and Resources Engineering, Fujian Key Laboratory of Eco-Industrial Green Technology, Wuyi University, Wuyishan, Fujian 354300 , Yu-Ling Wang† College of Chemistry and Chemical Engineering, Key Laboratory of Functional Small Molecules for Ministry of Education, Jiangxi Normal University, Nanchang, Jiangxi 330022 , Xue-Feng Zhang College of Chemistry and Chemical Engineering, Key Laboratory of Functional Small Molecules for Ministry of Education, Jiangxi Normal University, Nanchang, Jiangxi 330022 , Zhenjie Zhang College of Chemistry and State Key Laboratory of Medicinal Chemical Biology, Nankai University, Tianjin 300071 , Chun-Ting He College of Chemistry and Chemical Engineering, Key Laboratory of Functional Small Molecules for Ministry of Education, Jiangxi Normal University, Nanchang, Jiangxi 330022 and Qing-Yan Liu *Corresponding author: E-mail Address: [email protected] College of Chemistry and Chemical Engineering, Key Laboratory of Functional Small Molecules for Ministry of Education, Jiangxi Normal University, Nanchang, Jiangxi 330022 https://doi.org/10.31635/ccschem.021.202101575 SectionsSupplemental MaterialAboutAbstractPDF ToolsAdd to favoritesDownload CitationsTrack Citations ShareFacebookTwitterLinked InEmail The similarities in molecular size and physical properties of acetylene (C2H2) and carbon dioxide (CO2) produce a formidable challenge for their separation. Herein, we report two isoreticular fluorinated metal–organic frameworks (MOFs), labeled as JXNU-11(Fe2M) (M = Ni and Co), featuring unique octahedral cages encapsulated by cuboctahedral cages. JXNU-11(Fe2Ni) shows a record high C2H2-capture amount of 4.8 mmol g−1 and a long C2H2/CO2 breakthrough interval time of 55 min g−1 in an actual breakthrough experiment based on the equimolar C2H2/CO2 mixture under ambient conditions, indicating a high-performance material for C2H2 capture and C2H2/CO2 separation. Computational simulations revealed that the nanosized double-shell cages decorated with abundant fluorine and carboxylate oxygen atoms afford the optimized pore spaces for preferentially trapping C2H2, which account for the remarkable C2H2-capture capacity and the highly efficient C2H2/CO2 separation for JXNU-11(Fe2M). This work not only develops a design strategy for building the cage-in-cage structures in MOFs, but also provides universal guidance on designing porous MOFs with highly polarized and fluorophilic pore cages to capture C2H2. Download figure Download PowerPoint Introduction Acetylene (C2H2), the simplest alkyne, is an essential chemical for many common chemical products, such as acetaldehyde, acetic acid, plastic, and synthetic rubber,1 and electronic materials in the electronics industry.2 Additionally, C2H2 is an important flammable gas widely utilized for welding and metal cutting. The production of C2H2 from the oxidative coupling of natural gas is a commonly used preparation method for C2H2 gas in the petrochemical industry.3 Such a C2H2 preparation process leads to a small amount of carbon dioxide (CO2) in the C2H2 product. The presence of CO2 in C2H2 starting material has a seriously negative effect on subsequent preparation processes for the down-stream chemical products. Thus separation of C2H2/CO2 mixtures is vital in the petrochemical industry. However, the similar molecular sizes, as well as the same kinetic diameter (3.3 Å) of the linear-shaped C2H2 and CO2 molecules4–9 ( Supporting Information Table S1), cause the C2H2/CO2 separation to be a formidable task. Organic solvent extraction and cryogenic distillation are the current technologies for purifying C2H2 gas but are energy-intensive and environmentally unfriendly. Therefore, it is important to develop a highly energy-efficient and environment-friendly technology for achieving C2H2/CO2 separation. Metal–organic frameworks (MOFs) with porous and crystalline structures are fascinating porous solid materials.5–14 MOFs show highly promising potential in gaseous mixture separation due to their designable frameworks' structures and tunable pore environments.15–19 Recently, many MOFs have been utilized for the separation of C2H2/CO2 mixtures,20–29 and a few of them exhibit high-performance C2H2/CO2 separation.30–34 In the column breakthrough separation of binary gases, the breakthrough time and the captured amount for the late eluted adsorbate in the column are the important parameters for evaluating the separation efficiency of an adsorbent. The long breakthrough time for the late eluted gas generally results in a large captured amount for the late eluted gas, leading to a high separation efficiency of the adsorbent. However, in practice breakthrough experiments based on the equimolar C2H2/CO2 mixture, C2H2 breakthrough time for MOFs is generally shorter than 50 min g−1 under ambient conditions.35–40 The top-performing MOFs are SNNU-45 and ZJU-74a with the C2H2 breakthrough times of 113 and 81 min g−1,41,42 respectively. In contrast, the C2H2-captured amounts for MOFs in the packed columns are commonly less than 3 mmol g−1. SNNU-45 and ZJU-74a have the highest C2H2-capture amounts of 3.5 and 3.64 mmol g−1, respectively. It has been well demonstrated that the fluorine atoms of the inorganic anions, including MF62− (M = Si4+ and Ti4+) and NbOF52,− in the hybrid MOFs are the preferential bind sites for the acidic hydrogen atoms of the alkyne.43–47 The multiple C–H···F interactions between the C2H2 molecule and inorganic MF62− or NbOF52− groups of MOFs have resulted in an efficient C2H2/CO2 separation.47–49 Thus the fluorinated MOFs are a highly appealing platform for C2H2/CO2 separation. Unfortunately, due to the synthetic inaccessibility of the suitable fluorinated organic ligands, the fluorinated MOFs have thus been largely unexplored.50–54 Herein, we present two isostructural fluorous MOFs [termed as JXNU-11(Fe2M), M represents the divalent metal ions of Ni2+ and Co2+] with a fluorinated organic linker, featuring unique cage-in-cage structures. Remarkably, JXNU-11(Fe2Ni) shows a record-high C2H2-capture amount and a long C2H2 breakthrough time in the practice breakthrough experiment, resulting in high-performance C2H2/CO2 separation. The double-shell cages possessing highly electronegative F and O atoms in JXNU-11(Fe2M) are suitable pore cages to match the size of C2H2. The C2H2 molecules are trapped in the highly fluorophilic and polarized double-shell cages through strong host–guest interactions, which are responsible for the highly efficient C2H2/CO2 separation by JXNU-11(Fe2M). Experimental Section Synthesis of JXNU-11(Fe2Ni) A mixture of FeCl3·6H2O (8.10 mg, 0.03 mmol), Ni(NO3)3·6H2O (4.36 mg, 0.015 mmol), 3,3′,5,5′-tetrakis(fluoro)biphenyl-4,4′-dicarboxylate acid (4.71 mg, 0.015 mmol), 1,3,5-tris(4-carboxyphenyl)benzene (6.58 mg, 0.015 mmol), N,N-dimethylformamide (DMF) (2 mL), and CH3COOH (0.19 mL) was capped in a 20 mL vial and heated at 100 °C for 2 days. After cooling to room temperature, brown triangle-shaped crystals were obtained. Elemental analysis for {[Fe2Ni(μ3-O)(TFBPDC)(BTB)4/3(H2O)3]·6DMF·2.5H2O}n (C68H77F4O24.5N6Fe2Ni: 1616.74). Calcd/found: H, 4.80/4.71; C, 50.51/50.41; N, 5.19/5.02. IR data (KBr, cm−1): 3427 (m), 1662 (s), 1615 (s), 1394 (s), 1253 (w), 1185 (w), 1147 (w), 1098 (w), 1035 (s), 858 (s), 807 (w), 781 (s), 683 (w), 663 (w), 589 (m), 498 (m), 443 (s). Synthesis of JXNU-11(Fe2Co) A mixture of FeCl3·6H2O (8.10 mg, 0.03 mmol), Co(NO3)3·6H2O (4.37 mg, 0.015 mmol), 3,3′,5,5′-tetrakis(fluoro)biphenyl-4,4′-dicarboxylate acid (4.71 mg, 0.015 mmol), 1,3,5-tris(4-carboxyphenyl)benzene (6.58 mg, 0.015 mmol), DMF (2 mL), and CH3COOH (0.17 mL) was capped in a 20 mL vial and heated at 100 °C for 2 days. After cooling to room temperature, brown triangle-shaped crystals were obtained. Elemental analysis for {[Fe2Co(μ3-O)(TFBPDC)(BTB)4/3(H2O)3]·4DMF·H2O}n (C62H60F4O21N4Fe2Co: 1443.77). Calcd/found: H, 4.18/4.21; C, 51.57/51.46; N, 3.88/3.92. IR data (KBr, cm−1): 3420 (m), 1655 (s), 1612 (s), 1394 (s), 1254 (w), 1185 (w), 1146 (w), 1098 (w), 1034 (s), 859 (s), 808 (w), 781 (s), 706 (w), 663 (w), 589 (m), 500 (m), 443 (s). Methods X-ray single-crystal diffraction experiments were carried out with a Rigaku Oxford SuperNova diffractometer, and powder X-ray diffraction patterns were recorded on a Rigaku DMax 2500 powder diffractometer. Gas sorption–desorption isotherms were measured on a Micromeritics ASAP 2020 HD88 adsorption analyzer. Breakthrough experiments for separation of C2H2/CO2 (v/v, 50/50) were carried out in a fixed bed with a gas chromatograph detection system. The detailed experimental methods are provided in Supporting Information. Results and Discussion Compounds JXNU-11(Fe2M) constructed from the oxygen-centered heterometallic trimeric [Fe2M(μ3-O)(COO)6] (M = Ni2+ and Co2+) clusters (Figure 1a) were prepared. Compound JXNU-11(Fe2M) formulated as [Fe2M(μ3-O)(TFBPDC)(BTB)4/3(H2O)3]n is based on the linear 3,3′,5,5′-tetrakis(fluoro)biphenyl-4,4′-dicarboxylate (TFBPDC2−) and the triangular 1,3,5-tris(4-carboxyphenyl)benzene (BTB3−) ligands (Figure 1b) and was characterized by single-crystal X-ray diffraction ( Supporting Information Table S2). The phase purity of the bulk samples was confirmed by powder X-ray diffraction ( Supporting Information Figure S2). The metal concentrations in both compounds were determined by inductively coupled plasma atomic emission spectroscopy ( Supporting Information Table S3). The two compounds are isostructural and crystallize in a trigonal R3m space group. The trimeric [Fe2M(μ3-O)] core is coordinated by two TFBPDC2−, four BTB3−, and three water ligands ( Supporting Information Figure S1). Each [Fe2M(μ3-O)(COO)6] cluster is linked by four BTB3− ligands and two TFBPDC2− ligands to generate a three-dimensional (3D) framework. Exploration of the structure indicates the 3D framework contains two kinds of cages: a small octahedral cage formed from six [Fe2M(μ3-O)(COO)6] clusters, three TFBPDC2−, and four BTB3− ligands with a diameter of ∼12 Å (Figure 1c), and a large cage composed of 12 [Fe2M(μ3-O)(COO)6] clusters, six TFBPDC2−, and ten BTB3− ligands with a diameter of ∼26 Å, which can be described as a cuboctahedron (Figure 1d). Thus the 3D framework has close packing of the octahedral and cuboctahedral cages (Figure 1e). Such large voids in the cages in a single 3D framework lead to the generation of a twofold interpenetrated network (Figure 1f). It is remarkable that each octahedral cage is encapsulated by a large cuboctahedral cage from the interpenetrating network (Figure 1g). Such a unique cage-in-cage structure in a MOF is distinctive. The double-shell nested cages are reminiscent of the interesting Russian-doll-like cage. In addition, because of the presence of the highly polar C–F and C–O bonds and dense F atoms on the pore surfaces for these cages, double-shell nested cages exhibit highly polarized and fluorophilic character. As shown in Figure 1g, part of the voids in the large cuboctahedral cage are occupied by the small octahedral cage. The remaining pores of the total 3D framework are filled by the disordered guest solvent molecules, which occupy 64.1% and 65.6% of the volumes of unit cell for JXNU-11(Fe2Ni) and JXNU-11(Fe2Co), respectively. JXNU-11(Fe2M) materials exhibit excellent chemical stability after exposure to air for a long time or immersion in water with pH values ranging from 3 to 11 for 24 h ( Supporting Information Figure S3). The solvent-free JXNU-11(Fe2M) was obtained through solvent-exchange and heat under vacuum ( Supporting Information Figure S4). Figure 1 | Structures of JXNU-11(Fe2M). (a) [Fe2M(μ3-O)(COO)6] unit and (b) TFBPDC2− and BTB3− ligands. (c) 3D framework of JXNU-11(Fe2M). (d) Octahedral and (e) cuboctahedral cages. (f) Twofold interpenetrating frameworks of JXNU-11(Fe2M). (g) Cage-in-cage structure in JXNU-11(Fe2M). The fluorine atoms in (b–d) are represented as green balls. Download figure Download PowerPoint The permanent porosity of JXNU-11(Fe2M) was confirmed by N2 adsorption isotherms at 77 K. The N2 sorption isotherms for both compounds have typical type I sorption behavior with the saturation sorption amounts of 561 and 556 cm3 g−1 (Figure 2a). The pore volumes for JXNU-11(Fe2Ni) and JXNU-11(Fe2Co) from the experimental N2 data are 0.87 and 0.86 cm3 g−1, respectively, which are close to the corresponding crystal structure calculated values of 0.87 and 0.89 cm3 g−1. Additionally, the pore sizes are mainly around 6.8 and 11 Å (Figure 2a, inset), in good agreement with the obtained values from the crystal structures. The Brunauer–Emmett–Teller surface areas for JXNU-11(Fe2Ni) and JXNU-11(Fe2Co) were calculated to be 2208 m2 g−1 (Langmuir surface area of 2418 m2 g−1) and 2122 m2 g−1 (Langmuir surface area of 2392 m2 g−1) ( Supporting Information Figure S5), respectively. Figure 2 | Adsorption data of JXNU-11(Fe2M). (a) N2 adsorption–desorption isotherms at 77 K and pore size distribution for JXNU-11(Fe2M). C2H2 and CO2 adsorption–desorption isotherms of JXNU-11(Fe2M) at 273 K (b) and 298 K (c). Download figure Download PowerPoint The C2H2 and CO2 sorption isotherms of JXNU-11(Fe2M) (Figures 2b and 2c) were collected to evaluate the gas separation potentials for JXNU-11(Fe2M). JXNU-11(Fe2Ni) and JXNU-11(Fe2Co) exhibit high C2H2 adsorption capacities of 191 and 180 cm3 g−1 at 273 K and 1 bar, respectively, which are higher than the best-performance MOFs, including FJU-6-TATB (160 cm3 g−1),55 ATU-Cu (134 cm3 g−1),33 ZJU-74a (107 cm3 g−1),42 JXNU-10(Y) (94.9 cm3 g−1),27 CuI@UIO-66-(COOH)2 (71 cm3 g−1),56 and MOF-OH (68.7 cm3 g−1).57 At 298 K, the adsorption amounts of C2H2 are 118 and 107 cm3 g−1 for JXNU-11(Fe2Ni) and JXNU-11(Fe2Co), respectively, which are larger than those of the prominent MOFs FeNi-M′MOF (96 cm3 g−1),58 JNU-1 (63 cm3 g−1),59 NKMOF-1-Ni (61 cm3 g−1),60 UTSA-300a (69 cm3 g−1),47 and CPL-NH2 (41 cm3 g−1).39 In contrast, JXNU-11(Fe2M) showed low CO2 uptakes (Figures 2b and 2c). The high uptake of C2H2 is mainly caused by the polarized and fluorophilic microporous environments made of the cage-in-cage structures that are decorated with plenty of highly electronegative fluorine and carboxylate oxygen atoms that have high affinity for the acidic H atoms of C2H2 molecules but low affinity for CO2 molecules with two terminal electronegative O atoms. Such distinct gas sorption behaviors were confirmed by grand canonical Monte Carlo (GCMC) simulations. As depicted in Figures 3a and 3b, the distribution of C2H2 molecules in JXNU-11(Fe2M) is mainly within the octahedral cage and the space between the two cages, whereas much fewer CO2 molecules were distributed within the double-shell nest. Such a phenomenon suggests the double-shell nest is the desirable space for accommodating C2H2 molecules, in agreement with the experimental finding. The linear adsorption isotherms for CO2 further suggest the low affinity to CO2 for the host frameworks. The different adsorption behaviors between C2H2 and CO2 were also evidenced by the isosteric heats of adsorption (Qst) ( Supporting Information Figure S6). The obtained Qst of C2H2 were in the range of 31.6–29.7 kJ mol−1 for JXNU-11(Fe2M), which are notably higher than those of CO2 (16.0–19.6 kJ mol−1), further reflecting the strong affinity toward C2H2. The present Qst(C2H2) values are comparable to those of FJU-6-TATB (29 kJ mol−1),55 UTSA-74 (31 kJ mol−1),37 and JXNU-5a (32.9 kJ mol−1),35 but lower than those of CuI@UIO-66-(COOH)2 (74.5 kJ mol−1),56 JNU-1 (47.6 kJ mol−1),59 and NKMOF-1-Ni (53.9 kJ mol−1).60 The evident difference in adsorption enthalpy endows JXNU-11(Fe2M) with the thermodynamic separation possibility of a C2H2/CO2 mixture. Furthermore, JXNU-11(Fe2M) retained C2H2 storage ability after adsorption/desorption cycling experiments ( Supporting Information Figure S7), confirming their excellent recyclability for C2H2 adsorption. Figure 3 | Grand canonical Monte Carlo (GCMC) adsorption simulation. Computational C2H2 (a) and CO2 (b) distribution in the double-shell nest in JXNU-11(Fe2M) at 298 K and 1 atm. Download figure Download PowerPoint To evaluate the separation performance of JXNU-11(Fe2M), ideal adsorbed solution theory was used to calculate the separation selectivity of the C2H2/CO2 (v∶v = 50∶50) mixture. At 1 bar and 298 K, the adsorption selectivities for JXNU-11(Fe2Ni) and JXNU-11(Fe2Co) are 2.7 and 2.5, respectively ( Supporting Information Figure S8), which are comparable to the leading MOFs of UPC-200(Fe)-F-H2O (2.25)32 and FJU-6-TATB (3.1).55 The C2H2/CO2 uptake ratios for JXNU-11(Fe2Ni) and JXNU-11(Fe2Co) at 298 K and 1 bar are 2.1 and 1.9, respectively, which are larger than those of noted MOFs FJU-90a (1.75),36 SIFSIX-Cu-TPA (1.7),49 and ATU-Cu (1.2).33The high C2H2 adsorption capacity and moderate selectivity of JXNU-11(Fe2M) at ambient temperature reveal the greatly promising potential for C2H2/CO2 separation. To further investigate the C2H2/CO2 separation performance of JXNU-11(Fe2M), the breakthrough experiments were performed in practical separation processes for a C2H2/CO2 mixture (v∶v = 50∶50) at 298 K and 1 atm. The breakthrough experimental results show that CO2 was eluted first from the packed column, whereas C2H2 was retained in the bed for more than 120 and 108 min g−1 for JXNU-11(Fe2Ni) and JXNU-11(Fe2Co) (Figure 4a), respectively. The C2H2 breakthrough times for JXNU-11(Fe2M) rank among the leading MOFs ( Supporting Information Table S4). Moreover, the significant roll-up phenomenon of CO2 was observed in the breakthrough experiments, indicating a large proportion of previously adsorbed CO2 molecules can be replaced by the later fed C2H2 molecules. Such a phenomenon means that the C2H2 molecule competes better than CO2 for the binding sites of JXNU-11(Fe2M), highlighting the excellent separation efficiency of JXNU-11(Fe2M) for a C2H2/CO2 mixture. The breakthrough experiments were terminated when the concentrations of effluent gases stabilized. Figure 4 | C2H2 and CO2 separation performances. (a) Breakthrough curves of JXNU-11(Fe2M) at the flow of 2 mL min−1, 298 K, and 1 atm. Breakthrough curves of JXNU-11(Fe2Ni) at different temperatures (b) and different total flow rates at 298 K (c). Download figure Download PowerPoint The captured amounts for C2H2 during the 0∼tbreak time under the dynamic conditions are 4.8 and 4.3 mmol g−1 for JXNU-11(Fe2Ni) and JXNU-11(Fe2Co), respectively. The C2H2 captured amounts are remarkable and outperform all other MOFs, including the top-performing ZJU-74a (3.64 mmol g−1),42 SNNU-45 (3.5 mmol g−1),41 BSF-3 (2.9 mmol g−1),38 JCM-1 (2.2 mmol g−1),61 and FJU-90a (1.87 mmol g−1)36 (Figure 5 and Supporting Information Table S4). In addition, a long interval time of 55 min g−1 between C2H2 and CO2 breakthrough for JXNU-10(Fe2Ni) was obtained. Such an interval time stands out amongst MOFs and is only shorter than those of SNNU-45 (79 min g−1)41 and SIFSIX-Cu-TPA (69 min g−1).49 Furthermore, their practical separation potentials under different temperatures were evaluated. The C2H2 breakthrough times increased significantly with a decrease of temperature (Figure 4b and Supporting information Figure S9). The breakthrough times of C2H2 reached 146 (283 K) and 165 min g−1 (273 K) with a gas flow of 2 mL min−1. Figure 5 | Experimental breakthrough performance. Comparison of MOFs with top-high C2H2/CO2 breakthrough performance at 298 K and 1 atm. Download figure Download PowerPoint The separation performance of JXNU-11(Fe2M) with different gas flow rates at 298 K were also studied. With the gas flow of 2 mL min−1, the longest C2H2 breakthrough time and the largest amount of the adsorbed C2H2 were achieved for JXNU-11(Fe2M) (Figure 4c and Supporting Information Figure S10). JXNU-11(Fe2M) exhibited no appreciable changes in breakthrough times after three cycles of dynamic breakthrough experiments ( Supporting Information Figure S11), indicative of an excellent recycling separation capability. With the advantage of the modest adsorption heat of C2H2, JXNU-11(Fe2M) materials can be easily regenerated through purging the column with He gas at ambient temperature, as evidenced by the overlapped breakthrough curves ( Supporting Information Figure S11). Such results further indicate JXNU-11(Fe2M) are highly desirable microporous materials for C2H2/CO2 separation. Finally, the desorption experiments were carried out on JXNU-11(Fe2Ni). After reaching the breakthrough equilibrium, the adsorption column was purged with He gas (flow rate: 4 mL min−1) under ambient pressure and 303 K. As depicted in Figure 6a, the adsorbed CO2 molecules were released from the adsorption bed quickly. In contrast, the desorption of C2H2 gas was much slower. The productivity of C2H2 with over 95% purity was estimated from the desorption curve to be 1.98 mmol for 1 g of JXNU-11(Fe2Ni) (Figure 6b). Figure 6 | Breakthrough experiments. (a) and (b) Breakthrough curves and desorption curves of JXNU-11(Fe2Ni) based on the equimolar C2H2/CO2 mixture. Download figure Download PowerPoint To fully understand the underlying mechanism of the preferential adsorption of C2H2 over CO2 in JXNU-11(Fe2M), we performed comprehensive GCMC simulations to investigate the gas adsorption sites for JXNU-11(Fe2M). The calculated preferential binding sites of C2H2 are shown in Figures 7a and 7b. Four primary binding sites (sites I–IV) for C2H2 were found. As expected, the primary binding sites for C2H2 molecules are F and carboxylate O sites. For site I, site II, and site III, strong C−H···F hydrogen bonding notably occur between C2H2 and F atoms (H···F = 2.49–3.01 Å), which confirms the strong binding affinity of JXNU-11(Fe2M) toward C2H2. Compared with these sites, site IV exhibits strong C−H⋯O hydrogen bonds with a pair of carboxylate O atoms with the distances of 2.61 and 2.60 Å. These H⋯F and H⋯O distances are shorter than the sums of the corresponding van der Waals radii of hydrogen and fluorine (2.67 Å) or hydrogen and oxygen (2.72 Å) atoms, suggesting the substantial interactions. Moreover, the C≡C group of C2H2 interacts with the adjacent open metal sites through π⋯M interactions, and weakly interacts with the neighboring aromatic ring units of the framework through π⋯π interactions. Thus these multiple interactions between C2H2 molecules and the framework synergistically result in the remarkable affinity for C2H2. Therefore, the nanosized double-shell nests with many highly electronegative F and O atoms provide the polarized and fluorophilic pore spaces to accommodate C2H2. In contrast, the negatively charged F and O sites are not desirable sites for CO2. The presence of the repulsive interactions between the F/O atoms and the O atoms of CO2 leads to a weaker interaction between CO2 and the framework, which is consistent with the experimental results. The computational results gave an average binding energy of 31.8 kJ mol−1 for C2H2, which is much higher than that of 20.9 kJ mol−1 for CO2, further corroborating the stronger affinity toward C2H2 in the present framework. These calculated results clearly reveal that the rich F and O atoms as well as the open metal sites in the cage-in-cage structures are synergistically responsible for the preferential adsorption of C2H2 over CO2, thus affording the top-level C2H2/CO2 separation performance of JXNU-11(Fe2M). Figure 7 | Mechanism study. adsorption sites of C2H2 in JXNU-11(Fe2M). (a) I and (b) and Ni F and O in and H in C2H2. The labeled is measured in Å. Download figure Download PowerPoint two MOFs M = Ni and featuring nanosized structures and highly polarized and fluorophilic pore Such a cage-in-cage structure formed is composed of an and an large The double-shell nested cages in the MOFs provide the fascinating and the optimized pore spaces for trapping C2H2. The abundant F and O atoms of the organic ligands in JXNU-11(Fe2M) JXNU-11(Fe2M) with multiple binding sites for C2H2. The F and O atoms possessing high in JXNU-11(Fe2M) the pore surfaces of the cages result in the highly dense on the pore which are the desirable sites for trapping C2H2 with charged H atoms. As a JXNU-11(Fe2M) shows a strong binding affinity to C2H2 over CO2. The nanosized double-shell cages in JXNU-11(Fe2M) afford the optimized pore spaces for trapping C2H2, leading to an efficient C2H2/CO2 separation. The practical breakthrough performance of JXNU-11(Fe2Ni) the breakthrough time for C2H2 gas and the C2H2-capture the highest observed at ambient confirming the C2H2/CO2 separation performance of JXNU-11(Fe2M) Thus we a strategy for the design of cage-in-cage structures in MOFs and develop an efficient for the of the highly polarized and fluorophilic pore cages in the fluorous Supporting Information Supporting Information is and detailed experimental crystal data for JXNU-11(Fe2M), adsorption column breakthrough experiments, and GCMC simulation. of is no of to Information This work is by the of and and the for and of of Jiangxi of and of Acetylene and by the of K. Chemistry and of Metal–Organic and of Frameworks to MOF and on Adsorption in a as the in the of the Chemistry of and Metal–Organic Frameworks and Zhang of Frameworks Featuring Separation Metal–Organic Frameworks and for of Surfaces by in Synthesis of in a

We found that metal-organic framework (MOF) compounds M(2)(dhtp) (open metal M = Mg, Mn, Co, Ni, Zn; dhtp = 2,5-dihydroxyterephthalate) possess exceptionally large densities of open metal sites. By adsorbing one CH(4) molecule per open metal, these sites alone can generate very large methane storage capacities, 160-174 cm(3)(STP)/cm(3), approaching the DOE target of 180 cm(3)(STP)/cm(3) for material-based methane storage at room temperature. Our adsorption isotherm measurements at 298 K and 35 bar for the five M(2)(dhtp) compounds yield excess methane adsorption capacities ranging from 149 to 190 cm(3)(STP)/cm(3) (derived using their crystal densities), indeed roughly equal to the predicted, maximal adsorption capacities of the open metals (within +/-10%) in these MOFs. Among the five isostructural MOFs studied, Ni(2)(dhtp) exhibits the highest methane storage capacity, approximately 200 cm(3)(STP)/cm(3) in terms of absolute adsorption, potentially surpassing the DOE target by approximately 10%. Our neutron diffraction experiments clearly reveal that the primary CH(4) adsorption occurs directly on the open metal sites. Initial first-principles calculations show that the binding energies of CH(4) on the open metal sites are significantly higher than those on typical adsorption sites in classical MOFs, consistent with the measured large heats of methane adsorption for these materials. We attribute the enhancement of the binding strength to the unscreened electrostatic interaction between CH(4) and the coordinatively unsaturated metal ions.

A mesoporous metal−organic framework (MOF) material, UMCM-1, has been synthesized and characterized using N2 adsorption, powder X-ray diffraction, scanning electron microscopy, and Fourier transform infrared techniques. A detailed experimental study has been made of the adsorption of pure methane, hydrogen, carbon dioxide, oxygen, and nitrogen at various temperatures (298−338 K) and pressures (up to 25 bar). Multitemperature isotherms were modeled using the Dubinin−Astakhov equation to obtain useful thermodynamic properties including adsorption potential characteristic curves and isosteric heats of adsorption. Results are compared with mesoporous carbons and silicas. Large-pore materials are shown to exhibit relatively high heats of adsorption for CO2 when open metal sites are present. This phenomenon is not observed for methane, which indicates the importance of the CO2 quadrupole in influencing binding strength. Adsorption results for N2 and O2 show that selectivities in MOFs can be manipulated by the p...

Metal-organic frameworks (MOFs) with open metal sites have great potential for enhancing adsorption separation of the molecules with different polarities. However, the elution and separation of polar compounds on such MOFs packed columns using nonpolar solvents is difficult due to too strong interaction between polar compounds and the open metal sites. Here, we report the control of the coordination status of the open metal sites in MOFs by adjusting the content of methanol (MeOH) in the mobile phase for fast and high-resolution separation of polar compounds. To this end, high-performance liquid chromatographic separation of nitroaniline, aminophenol and naphthol isomers, sulfadimidine, and sulfanilamide on the column packed with MIL-101(Cr) possessing open metal sites was performed. The interaction between the open metal sites of MIL-101(Cr) and the polar analytes was adjusted by adding an appropriate amount of MeOH to the mobile phase to achieve the effective separation of the polar analytes due to the competition of MeOH with the analytes for the open metal sites. Fourier transform infrared spectra and X-ray photoelectron spectra confirmed the interaction between MeOH and the open metal sites of MIL-101(Cr). Thermodynamic parameters were measured to evaluate the effect of the content of MeOH in the mobile phase on the separation of polar analytes on MIL-101(Cr) packed column. This approach provides reproducible and high performance separation of polar compounds on the open metal sites-containing MOFs.

The development of new materials with high adsorption capacity and selectivity is becoming attractive for the applications of clean energy and environment pollution control. Metal-organic frameworks (MOFs) are promising adsorbents for gas storage and separation, such as H2 and CH4 storage, and CO2 capture, due to their extraordinarily high porosity, adjustable pore sizes, controllable surface functionality and potential scalability for industrial applications. This thesis focuses on developing novel MOFs for selective gas adsorption with large adsorption capacities and high selectivity, as well as good thermal and chemical stability. The studies include optimizing the activation conditions for uniform and empty pores with MOFs Cu-BTC taken as a case study, designing novel MOFs structure with desired functional groups for high selectivity of CO2 over other gases, fabricating MOFs contained composites with desired electrostatic force with ZIF-8/CNTs as an example, and evaluating the selective gas adsorption performance of all the prepared materials. This thesis aims to establish the relationship between the structure features of MOFs (pore size, metal centres, surface functional groups and electrostatic force) and gas adsorption performance of MOFs (including adsorption capacity and selectivity). The first part of experimental chapters focuses on the preparation and activation of copper-based MOFs Cu-BTC. The materials were synthesized by solvothermal method and activated by six different solvents (chloroform, dichloromethane, acetone, ethanol, methanol and water) in the activation process. The effects of different activation solvents on the thermal stability, porous structure and CO2 adsorption of Cu-BTC were investigated. The more DMF molecules were evacuated from the pores of Cu-BTC, the better adsorption performance was reflected in the material. The high crystalline and nearly solvent-free frameworks with highest BET surface area (2042 m2/g), largest pore volume (0.823 cm3/g) as well as highest CO2 loading (11.60 mmol/g at 0 dC and 132 kPa) can be achieved while using methanol as activation solvent. Then the selective adsorption of CO2/N2 and CO2/CH4 on Cu-BTC were examined through the experimental measurement of equilibrium adsorption capacities from pure fluids (CO2, CH4 and N2) and mixtures of CO2/N2 and CO2/CH4. Grand Canonical Monte Carlo (GCMC) model was performed to predict the adsorption capacities from pure fluids and binary mixtures. The GCMC model gives reasonable predictions of the measured adsorption capacities for pure gases at low pressures (l5 bar), but significantly over predicts that at pressures greater than 5 bar. The GCMC model fails to provide a satisfactory fit of the binary adsorption measurements across the entire pressure range studied. The Ideal Adsorbed Solution Theory (IAST) model using best-fit parameters for Langmuir isotherms of each pure fluid provides more satisfactory predictions of CO2/N2 and CO2/CH4 than the GCMC model. This combined experimental and modelling approach can provide criteria to screen MOFs for the separation of gas mixtures at industrially relevant compositions, temperatures and pressures. The second part of experimental chapters mainly focuses on synthesising MOFs with enhanced affinity for CO2 and selectivity of CO2 over other gases. Three novel amino-functionalized MOFs with both open metal sites (OMSs) and Levis basic sites (LBSs) were synthesized by solvothermal reactions. Single crystal structure analysis showed that Mg-ABDC and Co-ABDC were isostructural comprising two-dimensional layer structures, while Sr-ABDC contained a three-dimensional motif. These amino-functionalized MOFs were further characterized by powder X-ray diffraction, thermal gravimetric analysis and N2 ads-desorption. Adsorption isotherms of CO2 and N2 were obtained at various temperatures (0, 25 and 35 dC) and then the adsorption capacity and CO2/N2 selectivity for these MOFs were compared. Based on results, both Mg-ABDC and Co-ABDC decorated by the -NH2 groups and the open metal sites exhibit high heat of CO2 adsorption (g 30 kJ/mol) and excellent adsorption selectivity of CO2 over N2 (g375). In contrast, Sr-ABDC displays poor adsorption properties due to small pore size, low surface area and small pore volume. Introducing desired electrostatic force into MOF structures by the incorporation of carbon nanotubes (CNTs) into MOFs can obtain better crystals and enhance the properties of composite. A series of ZIF-8/CNTs composites were successfully synthesized by solvothermal method. The contents of ZIF-8 and CNTs in the composites were calculated from Thermogravimetric Analysis data. CO2 and N2 adsorption at 273 K on the composites were also investigated and compared. Results show that there are interactions (synergetic effect) between ZIF-8 crystals and CNTs in the composites, reflected in the change of crystallinity, morphology, thermal stability, and adsorption properties. The surface area and adsorption capacities of ZIF-8/CNTs composites can be controlled by adjusting the CNTs content in the composites. In optimal CNTs loading ratio, the ZIF-8/CNTs composite showed improved adsorption capacities and selectivity of CO2/N2, illustrating that the incorporation of CNTs into MOFs synthesis is a promising approach to enhance the adsorption performance of MOFs.

As a highly promising candidate for hydrogen storage, crucial to vehicles powered by fuel cells, metal–organic frameworks (MOFs) have attracted the attention of chemists in recent decades. H2 uptak...

Metal–Organic Frameworks (MOFs) with open metal sites (OMS) interact strongly with a range of polar gases/vapors. However, under ambient conditions, their selective adsorption is generally impaired due to a high OMS affinity to water. This led previously to the privilege selection of hydrophobic MOFs for the selective capture/detection of volatile organic compounds (VOCs). Herein, we show that this paradigm is challenged by metal(III) polycarboxylates MOFs, bearing a high concentration of OMS, as MIL‐100(Fe), enabling the selective capture of polar VOCs even in the presence of water. With experimental and computational tools, including single‐component gravimetric and dynamic mixture adsorption measurements, in situ infrared (IR) spectroscopy and Density Functional Theory calculations we reveal that this adsorption mechanism involves a direct coordination of the VOC on the OMS, associated with an interaction energy that exceeds that of water. Hence, MOFs with OMS are demonstrated to be of interest for air purification purposes.

Adsorption and separation of carbon dioxide and methane on different carbonaceous adsorbents were analyzed and compared. Coconut shell‐based activated carbon has the highest adsorption capacity for two gases. Sips model describes the adsorption isotherms best. The separation factor on coconut shell‐based activated carbon is the highest under various conditions, reaching about 3.8. The adsorption capacity of the two gases is closely related to the specific surface area and micropore volume of the adsorbent. The adsorbed amount of each component in the mixture is less than that of the pure component under the same condition, indicating that there is a competition in the adsorption process. The total adsorbed amount of the two gases decreases as the proportion of carbon dioxide decreases, implying that the adsorption process is dominated by carbon dioxide adsorption. Additionally, the separation factor decreases with increasing temperature. Understanding the adsorption behaviors of pure and binary carbon dioxide and methane is important in treating biomass gas using carbonaceous adsorbents.

In petroleum refining industries, the fracturing process allows for the cracking of long-chain hydrocarbons into a mixture of small olefin and paraffin molecules that are then separated via the energetically and monetarily demanding cryogenic distillation process. In an attempt to mitigate both energetic and capital consumptions, selective sorption of light hydrocarbons by tunable sorbents, such as metal-organic frameworks (MOFs), appears to be the most promising alternative for a more efficient gas separation process. MOFs are novel porous materials assembled from inorganic bricks connected by organic linkers. From a crystal engineering stand point, MOFs are advantageous in creating a range of microporous (0.2–2.0 nm) to mesoporous (>50 nm) void cavities, presenting unique opportunities for the functionalization of both the organic linkers and the void. Of significant importance is the MOF-74-M family (M = metal), characterized by a high density of open metal sites, that is not fully coordinated metal centers. This family of MOF is also known as CPO-27-M. MOF-74 have demonstrated more separation potential than other known MOFs and zeolites. Density functional theory (DFT), as implemented within a linear combination of atomic orbital (LCAO) approach, has been used to investigate the selective sorption of C1-C4hydrocarbons in MOF-74-Mg/Zn. The study was first implemented by adopting a molecular cluster approach, and later by applying periodic boundary conditions (PBC). While both modellistic approaches agree in showing significant differences in binding energies between olefins and paraffins adsorbed at the MOFs’ open metal sites, results reported at the molecular cluster level show underestimation when compared to those obtained at the PBC level. The use of PBC models allow for the correcting of binding energies for basis set superposition error (BSSE), molecular lateral interaction (LI), zero-point energy (ZPE), and thermal energy (TE) contributions. As such, results obtained at the PBC level are directly comparable to experimental calorimetric values (i.e., heat of adsorptions). This work discusses, for the first time, the origin of the fictitious agreement between binding energies obtained with molecular clusters and experimental heats of adsorption, identifying its origin as due to compensation of errors. Spectroscopy studies based on the intensities and frequency shifts with respect to the molecules in the gas phase are presented as a further investigation of the interaction of the small hydrocarbons (C1-C2) with the open metal sites in MOF-74-Mg. In an attempt to provide a more comprehensive description of the behavior of the hydrocarbon molecules, results from diffusion mechanism studies

The separation of light olefins from paraffins via cryogenic distillation is a very energy intensive process. Solid adsorbents and especially metal-organic frameworks with open metal sites have the potential to significantly lower the required energy. Specifically, M-MOF-74 has drawn considerable attention for application in olefin/paraffin separation. To investigate how the separation proceeds on a molecular level and to design better materials, molecular simulation can be a useful tool. Unfortunately, it is still a challenge to model the adsorption behavior of many adsorbates in metal-organic frameworks with open metal sites. Previously, the inclusion of explicit polarization has been suggested to improve the quality of classical force fields for such systems. Here, the potential of polarizable force fields for the description of olefins and paraffins in metal-organic frameworks with open metal sites is investigated. In particular, heats of adsorption, binding geometries, and adsorption isotherms are calculated for C2H4, C2H6, C3H6, and C3H8 in M-MOF-74 (with M = Co, Mn, Fe, and Ni). In this study, no force field parameters are adjusted to improve the model. The results show that including explicit polarization significantly improves the description of the adsorption in comparison to non-polarizable generic force fields which do not consider explicit polarization. The study also reveals that simulation predictions are sensitive to the assigned repulsive potential and framework charges. A fully re-parametrized polarizable force field may have the capability to improve the predictions even further.

We present a comprehensive investigation of the CO2 adsorption properties of an isostructural series of metal-organic frameworks, M-BTT (M = Cr, Mn, Fe, Cu; BTT3- = 1,3,5-benzenetristetrazolate), which exhibit a high density of open metal sites capable of polarizing and binding guest molecules. Coupling gas adsorption measurements with in situ neutron and X-ray diffraction experiments provides molecular-level insight into the adsorption process and enables rationalization of the observed adsorption isotherms. In particular, structural data confirms that the high initial isosteric heats of CO2 adsorption for the series are directly correlated with the presence of open metal sites and further reveals the positions and orientations of as many as three additional adsorption sites. Density functional theory calculations that include van der Waals dispersion corrections quantitatively support the observed structural features associated with the primary and secondary CO2 binding sites, including CO2 positions and orientations, as well as the experimentally determined isosteric heats of CO2 adsorption.

Efficient separation and storage of gas streams involving light hydrocarbons is essential for industrial applications. These hydrocarbons are widely used as energy resources and/or chemical raw materials in various chemical reactions. Here, we focus on the separation of acetylene from methane and carbon dioxide. The separation of acetylene from carbon dioxide is, in particular, challenging due to the similar kinetic diameters and boiling points of the molecules. In recent years, considerable progress has been made in adsorption-based separations using porous metal-organic frameworks (MOFs). Most reported studies are experimental. We present a computational study on these gas separations using a variety of MOFs. This allows investigation of the competitive gas adsorption, which is experimentally challenging, as well as understanding the adsorption mechanisms at the molecular level, which in turn allows further experimental MOF design for this application. MOFs with open metal sites, and particularly Fe-MOF-74, seem to be good for this separation, with a trade-off between physical adsorption capacity and selectivity. Based on experimental single-adsorption isotherms at various temperatures, we developed and validated a specific parameterization to account for the interactions of the olefin with the open metal sites. In addition to volumetric and calorimetric adsorption, we comprehensively investigate the characteristics of the interaction between the MOFs and the guest molecules in terms of binding sites and density profiles. The overall agreement of our simulated results with experimental data for pure components points to the reliability of the models and methods to successfully predict the separation of mixtures.

Metal-organic frameworks (MOFs) that contain open metal sites have the potential for storing hydrogen (H2) at ambient temperatures. In particular, Cu(I)-based MOFs demonstrate very high isosteric heats of adsorption for hydrogen relative to other reported MOFs with open metal sites. However, most of these Cu(I)-based MOFs are not stable in ambient conditions since the Cu(I) species display sensitivity toward moisture and can rapidly oxidize in air. As a result, researchers have focused on the synthesis of new air-stable Cu(I)-based materials for H2 storage. Here, we have developed a de novo synthetic strategy to generate a robust Cu(I)-based MOF, denoted as NU-2100, using a mixture of Cu/Zn precursors in which zinc acts as a catalyst to transform an intermediate MOF into NU-2100 without getting incorporated into the final MOF structure. NU-2100 is air-stable and displays one of the initial highest isosteric heats of adsorption (32 kJ/mol) with good hydrogen storage capability under ambient conditions (10.4 g/L, 233 K/100 bar to 296 K/5 bar). We further elucidated the H2 storage performance of NU-2100 using a combination of spectroscopic analysis and computational modeling studies. Overall, this new synthetic route may enable the design of additional stable Cu(I)-MOFs for next-generation hydrogen storage adsorbents at ambient temperatures.

Metal−organic frameworks (MOFs) with coordinatively unsaturated metal sites are appealing as adsorbent materials due to their tunable functionality and ability to selectively bind small molecules. Through the use of computational screening methods based on periodic density functional theory, we investigate O2 and N2 adsorption at the coordinatively unsaturated metal sites of several MOF families. A variety of design handles are identified that can be used to modify the redox activity of the metal centers, including changing the functionalization of the linkers (replacing oxido donors with sulfido donors), anion exchange of bridging ligands (considering μ-Br-, μ-Cl-, μ-F-, μ-SH-, or μ-OH- groups), and altering the formal oxidation state of the metal. As a result, we show that it is possible to tune the O2 affinity at the open metal sites of MOFs for applications involving the strong and/or selective binding of O2. In contrast with O2 adsorption, N2 adsorption at open metal sites is predicted to be relatively weak across the MOF dataset, with the exception of MOFs containing synthetically elusive V2+ open metal sites. As one example from the screening study, we predicted that exchanging the μ-Cl- ligands of M2Cl2(BBTA) (H2BBTA = 1H,5H-benzo(1,2-d:4,5-d′)bistriazole) with μ-OH- groups would significantly enhance the strength of O2 adsorption at the open metal sites without a corresponding increase in the N2 affinity. Experimental investigation of Co2Cl2(BBTA) and Co2(OH)2(BBTA) confirms that the former exhibits weak physisorption of both N2 and O2, whereas the latter is capable of chemisorbing O2 at room temperature in a highly selective manner. The O2 chemisorption behavior is attributed to the greater electron-donating character of the μ-OH- ligands and the presence of H-bonding interactions between the μ-OH- bridging ligands and the reduced O2 adsorbate.