Highly selective acetylene capture by a pacs-type metal-organic framework constructed using metal-formate complexes as pore partition units

Hongzhe GUO Sen WANG Lu YANG Fucheng LIU Jiongpeng ZHAO Zhaoquan YAO

Citation:  Hongzhe GUO, Sen WANG, Lu YANG, Fucheng LIU, Jiongpeng ZHAO, Zhaoquan YAO. Highly selective acetylene capture by a pacs-type metal-organic framework constructed using metal-formate complexes as pore partition units[J]. Chinese Journal of Inorganic Chemistry, 2025, 41(10): 2157-2164. doi: 10.11862/CJIC.20250179 shu

基于金属甲酸配合物作为孔分割单元构筑的pacs型金属有机框架的高选择捕获乙炔性能

    通讯作者: 刘福臣, fcliu@tjut.edu.cn
  • 基金项目:

    国家自然科学基金 22271217

    国家自然科学基金 22035003

    天津市自然科学基金 24JCYBJC00210

摘要: 为获得高效分离乙炔(C2H2)与二氧化碳(CO2)、乙烯(C2H4)的材料, 本研究以孔分割(PSP)策略为指导, 设计并合成了一例以金属甲酸配合物[In(FA)3Cl3]3-为孔分割单元的新型pacs型金属有机框架(MOF): (NH2Me2)2[Fe3(μ3-O)(bdc)3][In(FA)3Cl3] (Fe-FAIn-bdc), 其中bdc2-=对苯二甲酸根, FA-=甲酸根。通过金属-有机构筑单元[In(FA)3Cl3]3-的分割, 该配合物中具有丰富的限域空间。框架内氯原子与乙炔分子的强相互作用使该材料具有良好的C2H2/CO2分离性能。气体吸附实验显示, 在298 K和100 kPa下, 该材料对C2H2的吸附量为50.79 cm3·g-1, 显著高于同等温度下对CO2(29.99 cm3·g-1)和C2H4(30.94 cm3·g-1)的吸附量。基于理想吸附溶液理论(IAST)计算可知, 该材料对C2H2/CO2和C2H2/C2H4混合气体(体积比均为50∶50)的选择性分别为3.08和3.65, 超过部分已报道的MOFs材料(如NUM-11、SNNU-18等)。

English

  • Acetylene (C2H2) is a critical precursor for manufacturing essential polymers and industrial chemicals[1]. In industry, C2H2 is produced via methane combustion or hydrocarbon pyrolysis; during this process, carbon dioxide (CO2) is generated as a major impurity, which significantly affects the purity of the product[2]. Owing to the similar physical properties (i.e., boiling points, dipole moment, and polarizability), their separation is presently considered as one of the most challenging industrial separations. Although the conventional purification techniques, such as solvent extraction or cryogenic distillation, can achieve the separation, the high energy penalty and the environmental unsustainability of these methods hinder their further development and wide application[3]. Thus, developing an energy-efficient method for separating the C2H2/CO2 mixture is urgently desirable[4]. Adsorptive separation by using porous materials (porous carbon and zeolite) has emerged as one of the promising techniques for addressing acetylene purification. However, the almost same molecular geometry structure (linear shape) and the nearly identical molecular dimensions (C2H2: 0.332 nm×0.334 nm×0.57 nm; CO2: 0.318 nm×0.333 nm×0.536 nm) of these two gases bring huge challenges for selective physical adsorption[5].

    Compared to traditional porous materials, which only rely on physical adsorption mechanisms (e.g., molecular sieve effect), metal-organic frameworks (MOFs) have emerged as an ideal platform for fabricating the new generation adsorption materials owing to their superior structure programmability and pore environment modifiability[6]. By introducing additional binding sites or functional groups into the inner wall of the MOFs′ channels, it can not only achieve the precise pore size modification of these materials, but also endow these materials with intriguing chemical adsorption capacity based on improved host-guest interactions[7]. Over the past decade, a large number of porous MOFs with special functional groups have been constructed and exhibit great separation ability of the C2H2/CO2 mixture, relying on discriminatory gate effect, C—H⋯Cl hydrogen bonds, and the electrostatic interaction[8]. However, in most MOF systems, in an attempt to further enhance the separation performance of MOFs, blindly increasing the density of binding sites or functional groups in the framework always induces a dramatic decrease in the porosity, which finally results in the degradation of MOFs′ performance[9]. In order to break through the trade-off barrier between the density of functional groups in the framework and the free pore volume, a suitable MOF platform with ultra-high structure tunability is urgently desirable. Since 2013, Feng et al. have depended on the pore space partition (PSP) strategy, encapsulating a series of pore partition agents with C3 symmetric into the 1D channels of MIL-88 to form the famous pacs-MOFs[10], which can be an ideal platform for fabricating the MOF-based adsorption materials. Firstly, in this system, the 1D open channel spaces in original MOFs (MIL-88) can be rationally divided into numerous smaller segments to form the confined spaces, which have beneficial effects for enhancing the interactions between the host framework and guest gas molecules[11]. Secondly, because this type of structure was integrated by the trinuclear metal cluster, linear bidentate carboxyl ligands, and the tridentate N-containing ligands with C3 symmetric, the pacs-MOFs exhibit some advantages such as the fruitful species of building blocks, the highly structural designability and programmability, which is convenient for subsequent modification of functional groups and active sites[12]. The last, the synergistic effect between different functional groups or active sites in the regular confined space (cages with trigonal bipyramidal geometry and cylindrical geometry) of pacs-MOFs has significant positive effects for improving the adsorption selectivity of materials[13]. Up to date, most of the pacs-MOFs were constructed by using organic pyridinyl ligands, which extremely limited the structural diversity of pacs-MOFs. In contrast, utilizing the simple organic molecules (i.e., isonicotinic acid, triazole, and formic acid) to design and construct the novel metal-organic pore-partition ligands not only increases the structural diversity of this type of MOFs, but also improves the modifiability of the framework. However, the relative research remains scarcely reported[14].

    Inspired by the above mentions, in this work, a novel pacs-MOF (NH2Me2)[Fe3(μ3-O)(bdc)3][In(FA)3Cl3] (denoted Fe-FAIn-bdc; bdc2-=terephthalate) was constructed successfully by using [In(FA)3Cl3]3- (FA-=formate) as pore-partition agents through the solvothermal method. Distinguished from the common planar triangular organic N-containing ligands, the [In(FA)3Cl3]3- exhibits a stereo configuration and two-fold orientational disordered state in the network of Fe-FAIn-bdc. The abundant Cl- anions in this unit can act as potential binding sites, which could significantly enhance the adsorption capacity for C2H2 via host-guest interactions, finally improving the selectivity of Fe-FAIn-bdc for C2H2/CO2. The adsorption data illustrate that the adsorption capacity of Fe-FAIn-bdc for C2H2 and CO2 was about 50.79 cm3·g-1 and 29.99 cm3·g-1 at 298 K and 100 kPa with a high C2H2/CO2 selectivity of 3.08 in a volume ratio of 50∶50.

    The reagents and instruments are listed in the supporting information, as well as the activation and gas adsorption tests of the materials.

    Synthesis of Fe-FAIn-bdc. FeCl2·4H2O (0.2 mmol, 40 mg), InCl3 (0.1 mmol, 22 mg), and H2bdc (0.2 mmol, 33 mg) were dissolved in the mixture of 4.0 mL of N, N-dimethylformamide (DMF) with 0.3 mL 50% HBF4. The mixture was sealed in a 10 mL glass vial and was heated in an oven at 120 ℃ for 2 d without disturbance. After the reaction system was cooled to room temperature, the orange-red strip-shaped crystals were obtained after filtration, washed with DMF several times, and dried in air. Yield: 23% (based on InCl3).

    The orange-red strip-shaped crystals of Fe-FAIn-bdc, formulated as (NH2Me2)2[Fe3(μ3-O)(bdc)3][In(FA)3 Cl3], was synthesized by mixing a solution FeCl2·4H2O, InCl3, H2bdc and HBF4 under solvothermal reaction at 120 ℃ for 2 d. Single-crystal X-ray diffraction analysis reveals that Fe-FAIn-bdc crystallizes in the hexagonal P63/mmc space group belonging to 6/mmm point group (Table 1). The asymmetric unit contains one Fe3+ ion (Fe1), one-third of a bridged μ3-O2- ion, one bdc2- anion, one formate anion, 1/3 of a In3+ cation, one Cl- anion, and 2/3 of a dimethyl ammonium cation with three-fold disorder. To confirm the valence state of Fe elements, the bond valence calculation was carried out, demonstrating that the bond valence sum analysis of Fe1 in Fe-FAIn-bdc was 3.028 7, which was very close to 3, by using r0=0.176 5 nm for Fe3+ ions and 2.785 3 by using r0=0.173 4 nm for Fe2+ ions[15-16]. This result indicates that the valence state of Fe1 should be trivalent. Each Fe3+ ion exhibits a distorted octahedral coordination sphere with four O atoms from four bdc2- ligands in the equatorial plane, one O atom from the formate anion, and one μ3-O2- anion on the axial positions. Three crystallographically equivalent Fe3+ ions are interconnected via a μ3-O2- group and further coordinate with the carboxyl groups of bdc2- ligands to form the classical [Fe3(μ3-O)(COO)6]+ trinuclear metal cluster (Fig.1a and 1b). The adjacent trinuclear in space are connected with each other by bdc2- ligands to construct the famous MIL-88-type framework with acs topology, featuring the large 1D hexagonal channels and fruitful open metal sites along the c-axis (Fig.1c and 1e). Then, the open metal sites on the inner wall of the channels are occupied by the metal-organic pore-partition ligands [In(FA)3Cl3]3-. In this unit, the In3+ ions (In1) exhibit an octahedral coordination model with three O atoms from three formate anions and three Cl- anions. Along the c-axis direction, the whole geometric structure of [In(FA)3Cl3]3- units is like an equilateral triangle with C3-symmetric, which is very similar to the classical pore-partition organic ligands [i.e., tri(pyridin-4-yl)amine (TPA), 2,4,6-tri(4-pyridyl)-1,3,5-triazine (TPT)]. After that, the 1D open channels of MIL-88 were fragmented into numerous segments to form the typical structure of pacs-MOFs (Fig.1d and 1f).

    Table 1

    Table 1.  Crystallographic data of Fe-FAIn-bdc
    下载: 导出CSV
    Parameter Fe-FAIn-bdc
    Formula C33H36O19N3Cl3Fe3In
    Formula weight 1 167.41
    Temperature / K 293(2)
    Crystal system Hexagonal
    Space group P63/mmc
    a / nm 1.320 66(12)
    b / nm 1.320 66(12)
    c / nm 1.827 67(17)
    Volume / nm3 2.760 6(6)
    Z 2
    μ / mm-1 1.392
    F(000) 1 170.0
    Reflection collected 4 404
    Independent reflection 959
    Goodness-of-fit on F2 1.708
    Final R indexes [I≥2σ(I)] R1=0.10 87, wR2=0.322 9
    Final R indexes (all data) R1=0.143 6, wR2=0.394 4

    Figure 1

    Figure 1.  (a) Connection mode diagram of Fe-FAIn-bdc; (b) Structural schematic diagram of Fe3-clusters; (c) Peripheral framework structure (MIL-88) constructed by Fe3-clusters and bdc2- ligands; (d) Crystal structure of Fe-FAIn-bdc along the c-axis; (e) View of the 1D channels of the peripheral framework along a- or b-axis; (f) Small segments of Fe-FAIn-bdc after fragmented the infinite 1D channel in MIL-88 by [In(FA)3Cl3]3- ligands; (g) Trigonal bipyramid cages in Fe-FAIn-bdc which constructed by six bdc2- ligands and five Fe3-clusters

    Symmetry codes: i 1-y, 1-x, 1/2-z; ii 1-y, 1-x, z; iii x, y, 1/2-z; iv 1-y, -1+x-y, z; v 2+y-x, 1-x, z.

    Owing to the two-fold disordered state of the formate anions, the window size of Fe-FAIn-bdc is only about 0.472 nm, which is much smaller than that in traditional pacs-MOFs. The whole framework is anionic, and two dimethyl ammonium cations, which exhibit a three-fold disorder state, are located near the Fe3-clusters to balance the surplus negative charges. In this structure, two types of nanocage structures with different geometric shapes can be found (Fig.1f and 1g). One cage exhibits trigonal bipyramidal geometry with spherical diameters of ca. 1.827 and 1.452 nm, which was constructed by six bdc2- ligands and five Fe3-clusters. Compared to traditional TPA-based pacs-MOFs, the [In(FA)3Cl3]3- units significantly obstruct the triangular apertures of the trigonal bipyramidal cages. The other cage exhibits regular cylindrical geometry, which was assembled by six bdc2- ligands and two [In(FA)3Cl3]3- units. The height and width of this cage are 0.913 and 1.320 nm, respectively, indicating the abundant free space in this confined space. Besides, all the Cl- anions in [In(FA)3Cl3]3- are toward the center of this cage, which is beneficial for capturing C2H2 molecules in this narrow confined space through multiple C—H⋯Cl interactions. According to the calculation results of PLATON software, the effective free volume of this Fe-FAIn-bdc is about 33.9%, upon removal of internal guest molecules, which accounts for the spatial occupancy of the In-based structures[17-19]. The fruitful internal confined spaces, which are decorated by Cl- anions, and the narrow pore size along the a- or b-axis endow this MOF with potential application perspectives in the field of gas separations.

    The phase purity and the chemical/thermal stability of Fe-FAIn-bdc were confirmed by powder X-ray diffraction (PXRD) and thermogravimetric analysis (TGA). As shown in Fig.2a, the experimental PXRD pattern could match well with the simulation result, demonstrating the high purity of the crystal powder sample of Fe-FAIn-bdc. Besides, after being immersed in some common organic solvents (i.e., CH2Cl2, MeOH, and acetone) for 24 h, the sample of Fe-FAIn-bdc could still maintain the framework intact. On the contrary, most of the diffraction peaks in the PXRD pattern of the sample immersed in water for 24 h disappeared, suggesting its poor stability in water. According to the TGA curves of Fe-FAIn-bdc before and after solvent exchange by acetone, the framework could remain stable until about 200 ℃. The obvious weight loss before 200 ℃ can be attributed to the removal of the solvent molecules, which are encapsulated in the network of Fe-FAIn-bdc (Fig.2b)

    Figure 2

    Figure 2.  (a) PXRD patterns of the crystal powder sample of Fe-FAIn-bdc after being immersed in different common solvents; (b) TGA curves of Fe-FAIn-bdc and the sample exchanged by acetone

    To investigate the permanent porosity of Fe-FAIn-bdc, the N2 adsorption-desorption experiment of Fe-FAIn-bdc at 77 K was measured. However, owing to the narrow pore size of Fe-FAIn-bdc and the dramatic thermal vibration of formate anions near the window of the internal space, Fe-FAIn-bdc didn′t exhibit obvious N2 adsorption behavior at 77 K (Fig.S1). Miraculously, Fe-FAIn-bdc exhibited remarkable CO2 adsorption performance at 298 K and 100 kPa. The CO2 adsorption uptake of Fe-FAIn-bdc reached 29.99 cm3·g-1 (Fig.3a), which can be attributed to the smaller kinetic diameter of CO2 (0.33 nm) compared to N2 (0.364 nm) and the larger polarizability and stronger quadrupole moment of CO2 molecules. These results inspired us to investigate the adsorption capacity of Fe-FAIn-bdc to C2H2, which has a similar kinetic diameter to CO2 (0.33 nm). As shown in Fig.3a, under same condition (298 K and 100 kPa) the adsorption uptake of C2H2 on Fe-FAIn-bdc reached up to 50.79 cm3·g-1, which was much higher than that of CO2 with a large uptake ratio of 169%, surpassing many benchmark MOFs such as TIFSIX-2-Cu-i (95%)[20] and SIFSIX-3-Ni (120%)[20], rivaling UTSA-74-Zn (150%)[21]. Besides, the adsorption isotherms curve of Fe-FAIn-bdc for C2H4 has also been obtained and the adsorption uptake was only about 30.94 cm3·g-1 at 298 K and 100 kPa (Fig.3b). In addition, compared with the slowly increasing trend of CO2 or C2H4 uptake over the whole pressure region, the C2H2 adsorption uptake of Fe-FAIn-bdc increased dramatically in a p/p0 range of 0-0.3, which indicates the stronger interaction between host framework and C2H2 molecules.

    Figure 3

    Figure 3.  (a) Adsorption isotherms of Fe-FAIn-bdc for CO2 and C2H2 at 298 K; (b) Adsorption isotherms of Fe-FAIn-bdc for C2H2 and C2H4 at 298 K

    To evaluate the separation ability of Fe-FAIn-bdc for the mixture of C2H2/CO2 and C2H2/C2H4, the ideal adsorbed solution theory (IAST) was employed to estimate the adsorption selectivity for C2H2/CO2 and C2H2/C2H4 in volume ratio of 50∶50. By fitting the isotherms according to the dual-site Langmuir-Freundlich equation, the selectivity of Fe-FAIn-bdc for C2H2/CO2 (50∶50) was calculated to be 3.08 (Fig.S2) at 298 K and 100 kPa. This value was much higher than some reported benchmark MOFs such as Co-MOF-1 (2.1), SNNU-18 (2.8), and NUM-11 (3) but still lower than some famous MOFs such as UTSA-220 (4.4) and MUF-17 (6.01) (Table S1 and Fig.4a). Compared with the high selectivity of Fe-FAIn-bdc for C2H2 /CO2 (50:50), the selectivity for C2H2/C2H4 (50∶50) has also been calculated. The value (3.65) (Fig.S3) was higher than some reported MOF materials (i.e., SNNU-95 and MOF-74-Fe), but still couldn′t match well with most top-performing C2H2/C2H4 separation materials (SIFSIX-2-Cu) (Table S2 and Fig.4b)[21]. The relatively high selectivity of Fe-FAIn-bdc for C2H2/CO2 (50∶50) and C2H2/C2H4 (50∶50) makes this MOF a good candidate for application in the field of purification of acetylene in industry.

    Figure 4

    Figure 4.  (a) Comparison about C2H2/CO2 selectivity and C2H2 capacity of representative MOFs at 298 K and 100 kPa; (b) Comparison about C2H2/C2H4 selectivity and C2H2 capacity of representative MOFs at 298 K and 100 kPa

    The references are listed in the Supporting information.

    In summary, based on the reticular chemistry and the pore space partition (PSP) strategy, a novel pacs-MOFs (Fe-FAIn-bdc) was constructed successfully by solvothermal method. Distinguished from the traditional organic pyridyl pore-partition ligands with C3 symmetry, in this complex, the metal-formate complex [In(FA)3Cl3]3- unit acts as the pore-partition agent to participate in the self-assembly process of Fe-FAIn-bdc. On account of the small pore size and large pore volume of Fe-FAIn-bdc and the fruitful confined space which was decorated by Cl- anions, this MOF presented a high C2H2 adsorption capacity of 50.79 cm3·g-1 at 298 K and high IAST selectivity of 3.08 for C2H2/CO2 and 3.65 for C2H2/C2H4. This work not only provide a new example of C2H2 purification adsorbents, but also sheds new light on the design of novel pacs-MOFs with metal-organic pore-partition agents.


    Supporting information is available at http://www.wjhxxb.cn
    1. [1]

      FLORIAN M, IVAN D S, NADA H S, TIMOTHY L S, MATHEW S, HARRY G G, STEWART F P, PASCAL M, YANG S H, MARTIN S. Unravelling exceptional acetylene and carbon dioxide adsorption within a tetra-amide functionalized metal-organic framework[J]. Nat. Commun., 2017, 8: 14085 doi: 10.1038/ncomms14085

    2. [2]

      OSAMAH A, LIN R B, WANG H L, LI B, HADI D A, HUT L, CHEN B L. Metal-organic framework with trifluoromethyl groups for selective C2H2 and CO2 adsorption[J]. Cryst. Growth Des., 2018, 18: 4522-4527 doi: 10.1021/acs.cgd.8b00506

    3. [3]

      XIE Y, CUI H, WU H, LIN R B, ZHOU W, CHEN B L. Electrostatically driven selective adsorption of carbon dioxide over acetylene in an ultramicroporous material[J]. Angew. Chem.‒Int. Edit., 2021, 60: 9604-9609 doi: 10.1002/anie.202100584

    4. [4]

      NIU Z, CUI X L, TONY P, GAURAV V, LAN P C, CHUAN S, XING H B, KATHERINE F, SHANELLE S, BRIAN S, AYMAN N, ABDULLAH A, MA S Q. A MOF-based ultra-strong acetylene nano-trap for highly efficient C2H2/CO2 separation[J]. Angew. Chem.‒Int. Edit., 2021, 60: 5283-5288 doi: 10.1002/anie.202016225

    5. [5]

      LU T T, FAN Y Y, WANG X N, WANG Q, BAO L. A microporous chromium-organic framework fabricated via solvent-assisted metal metathesis for C2H2/CO2 separation[J]. Dalton Trans., 2022, 51: 11658-11664 doi: 10.1039/D2DT01546C

    6. [6]

      WANG K Y, HUANG H C, ZHANG X Y, ZHAO G S, LI F T, GU Y F. Designed metal-organic frameworks with potential for multicomponent hydrocarbon separation[J]. Coord. Chem. Rev., 2023, 484: 215111 doi: 10.1016/j.ccr.2023.215111

    7. [7]

      ZHAO X, WANG Y X, LI D S, BU X H, FENG P Y. Metal-organic frameworks for separation[J]. Adv. Mater., 2018, 30(37): 1705189 doi: 10.1002/adma.201705189

    8. [8]

      ZHANG Z Q, SHING B P, WANG Y X, KANG C J, FAN W D, ZHAO D. Efficient trapping of trace acetylene from ethylene in an ultramicroporous metal-organic framework: Synergistic effect of high-density open metal and electronegative sites[J]. Angew. Chem.‒Int. Edit., 2020, 59: 18927-18932 doi: 10.1002/anie.202009446

    9. [9]

      XUE Y Y, BAI X Y, ZHANG J, WANG Y, LI S N, JIANG Y C, HU M C, ZHAI G Q. Precise pore space partitions combined with high-density hydrogen-bonding acceptors within metal-organic frameworks for highly efficient acetylene storage and separation[J]. Angew. Chem.‒Int. Edit., 2021, 60: 10122-10128 doi: 10.1002/anie.202015861

    10. [10]

      YANG H J, PENG F, HONG A N, WANG Y X, BU X H, FENG P Y. Ultrastable high-connected chromium metal-organic frameworks[J]. J. Am. Chem. Soc., 2021, 143: 14470-14474 doi: 10.1021/jacs.1c07277

    11. [11]

      ZHAI Q G, BU X H, ZHAO X, LI D S, FENG P Y. Pore space partition in metal-organic frameworks[J]. Accounts Chem. Res., 2017, 50: 407-417 doi: 10.1021/acs.accounts.6b00526

    12. [12]

      ZHAI Q G, BU X H, MAO C Y, ZHAO X, DAEMEN L, CHENG Y Q, RAMIREZ A J, FENG P Y. An ultra-tunable platform for molecular engineering of high-performance crystalline porous materials[J]. Nat. Commun., 2016, 7: 13645 doi: 10.1038/ncomms13645

    13. [13]

      XIAO Y C, HONG A N, CHEN Y H. YANG H J, WANG Y X, BU X H, FENG P Y. Developing water-stable pore-partitioned metal-organic frameworks with multi-level symmetry for high-performance sorption applications[J]. Small, 2023, 19: 2205119 doi: 10.1002/smll.202205119

    14. [14]

      ZHAO X, BU X H, NGUYEN E T, ZHAI Q G, MAO C Y, FENG P Y. Multivariable modular design of pore space partition[J]. J. Am. Chem. Soc., 2016, 138: 15102-15105 doi: 10.1021/jacs.6b07901

    15. [15]

      SHELDRICK G M. Crystal structure refinement with SHELXL[J]. Acta Crystallogr. Sect. C, 2015, C71: 3-8

    16. [16]

      PACIOREK W A, MEYER M, CHAPUIS G. On the geometry of a modern imaging diffractometer[J]. Acta Crystallogr. Sect. A, 1999, A55: 543-557

    17. [17]

      BOURHIS L J, DOLOMANOV O V, GILDEA R J, HOWARD J A K, PUSCHMANN H. The anatomy of a comprehensive constrained, restrained refinement program for the modern computing environment-Olex2 dissected[J]. Acta Crystallogr. Sect. A, 2015, A71: 59-75

    18. [18]

      DEPMEIER W, BÜHRER W. Aluminate sodalites: Sr8[Al12O24](MoO4)2(SAM) at 293, 423, 523, 623 and 723 K and Sr8[Al12O24](WO4)2(SAW) at 293 K[J]. Acta Crystallogr. Sect. B, 1991, B47: 197-206

    19. [19]

      LIU W T, THORP H H. Bond valence sum analysis of metal-ligand bond lengths in metalloenzymes and model complexes. 2. Refined distances and other enzymes[J]. Inorg. Chem., 1993, 32: 4102-4105 doi: 10.1021/ic00071a023

    20. [20]

      CUI X L, CHEN K J, XING H B, YANG Q W, RAJAMANI K, BAO Z B, WU H, ZHOU W, DONG X L, HAN Y, LI B, REN Q L, MICHAEL Z, CHEN B L. Effect of pore chemistry and size control in hybrid porous materials for acetylene capture from ethylene[J]. Science, 2016, 353: 141-144 doi: 10.1126/science.aaf2458

    21. [21]

      XIAO Y Q, LI S H, JIANG B, LIANG X M, CHU Y Y, DENG F. Effect of co-adsorbed guest adsorbates on the separation of ethylene/ethane mixtures on metal-organic frameworks with open metal sites[J]. Chem.‒Eur. J. 2024, 30: 20241006

  • Figure 1  (a) Connection mode diagram of Fe-FAIn-bdc; (b) Structural schematic diagram of Fe3-clusters; (c) Peripheral framework structure (MIL-88) constructed by Fe3-clusters and bdc2- ligands; (d) Crystal structure of Fe-FAIn-bdc along the c-axis; (e) View of the 1D channels of the peripheral framework along a- or b-axis; (f) Small segments of Fe-FAIn-bdc after fragmented the infinite 1D channel in MIL-88 by [In(FA)3Cl3]3- ligands; (g) Trigonal bipyramid cages in Fe-FAIn-bdc which constructed by six bdc2- ligands and five Fe3-clusters

    Symmetry codes: i 1-y, 1-x, 1/2-z; ii 1-y, 1-x, z; iii x, y, 1/2-z; iv 1-y, -1+x-y, z; v 2+y-x, 1-x, z.

    Figure 2  (a) PXRD patterns of the crystal powder sample of Fe-FAIn-bdc after being immersed in different common solvents; (b) TGA curves of Fe-FAIn-bdc and the sample exchanged by acetone

    Figure 3  (a) Adsorption isotherms of Fe-FAIn-bdc for CO2 and C2H2 at 298 K; (b) Adsorption isotherms of Fe-FAIn-bdc for C2H2 and C2H4 at 298 K

    Figure 4  (a) Comparison about C2H2/CO2 selectivity and C2H2 capacity of representative MOFs at 298 K and 100 kPa; (b) Comparison about C2H2/C2H4 selectivity and C2H2 capacity of representative MOFs at 298 K and 100 kPa

    The references are listed in the Supporting information.

    Table 1.  Crystallographic data of Fe-FAIn-bdc

    Parameter Fe-FAIn-bdc
    Formula C33H36O19N3Cl3Fe3In
    Formula weight 1 167.41
    Temperature / K 293(2)
    Crystal system Hexagonal
    Space group P63/mmc
    a / nm 1.320 66(12)
    b / nm 1.320 66(12)
    c / nm 1.827 67(17)
    Volume / nm3 2.760 6(6)
    Z 2
    μ / mm-1 1.392
    F(000) 1 170.0
    Reflection collected 4 404
    Independent reflection 959
    Goodness-of-fit on F2 1.708
    Final R indexes [I≥2σ(I)] R1=0.10 87, wR2=0.322 9
    Final R indexes (all data) R1=0.143 6, wR2=0.394 4
    下载: 导出CSV
  • 加载中
计量
  • PDF下载量:  2
  • 文章访问数:  74
  • HTML全文浏览量:  13
文章相关
  • 发布日期:  2025-10-10
  • 收稿日期:  2025-05-30
  • 修回日期:  2025-08-28
通讯作者: 陈斌, bchen63@163.com
  • 1. 

    沈阳化工大学材料科学与工程学院 沈阳 110142

  1. 本站搜索
  2. 百度学术搜索
  3. 万方数据库搜索
  4. CNKI搜索

/

返回文章