Chao-Ying
Gao‡
*ab,
Chen
Mao‡
ab,
Yang
Yang
a,
Ning
Xu
a,
Jinglin
Liu
a,
Xiaohong
Chen
a,
Jinghai
Liu
*ab and
Limei
Duan
*ab
aCollege of Chemistry and Materials Science, Inner Mongolia Minzu University (IMMN), Tongliao 028043, Inner Mongolia, People's Republic of China. E-mail: chaoyinggao@163.com; jhliu2008@sinano.ac.cn; duanlmxie@126.com
bInner Mongolia Key Lab of Carbon Nanomaterials, Nano Innovation Institute (NII), Inner Mongolia Minzu University (IMMN), Tongliao 028000, People's Republic of China
First published on 10th November 2022
Hydrothermal reaction of silver nitrate and a tetraphosphonic acid (H8L) affords a novel coordination polymer, with the general formula, [Ag10(H3L)2(H2O)2(4,4′-bipy)], denoted as compound 1. It is built from extended ⋯Ag–O–P–O⋯ chains and organic linkers to form a 3D network. In its structure, three of four phosphonyl groups of the organic ligand are protonated, endowing compound 1 with rich Brønsted acid sites. With Brønsted and Lewis acidic sites, the catalytic activity of 1 was investigated through cycloaddition reaction of CO2 and epoxides, and the results displayed an excellent performance. Besides, the heterogeneous nature of compound 1 was proved by five cycle experiments with no significant compromise on the activity, indicating the silver phosphonate as an excellent catalyst for CO2 chemical fixation.
Silver catalysts are widely used in both organic reactions and the chemical industry as Lewis acids.7–9 Due to their d10 specific electronic configuration, silver catalysts have shown a characteristic σ- and/or π-activation in discrete reactions.10–12 Recently, heterogeneous silver-based catalysts by immobilization of silver nanoparticles or silver atoms into porous MOFs have been reported.13–15 Ag@MOF composites are usually prepared by multi-step postsynthesis under strongly acidic or strongly oxidizing conditions (such as concentrated sulfuric acid and concentrated nitric acid). Such harsh conditions can only be applied to very few ultra-stable MOFs (such as Cr-MIL-101, UiO-66, etc.).13,14 Meanwhile, it is difficult to explore the relevant catalytic mechanism for composite catalysts due to the lack of intuitive structural characterization (such as single crystal X-ray diffraction analysis). The above shortcomings are considered to be avoided by building up Ag(I) node based MOF catalysts: (1) the geometric coordination configuration of the Ag(I) sites can be intuitively determined; (2) the synthesis conditions are mild and the operation is simple. However, the stability of such materials have always puzzled chemists: Ag(I) metal centers usually undergo hydrolysis and lead to the degeneration of catalysts.16 Therefore, the application of MOFs with Ag(I) nodes in the field of heterogeneous catalysis is still relatively rare.10,11
Considering the advantages of metal phosphonates on structural stability and diversity and the excellent specific activation ability of Ag(I) compounds, it is very meaningful to develop Ag(I) phosphonates and apply them in heterogeneous catalysis. Herein, H8L ((ethene-1,1,2,2-tetrayltetrakis(benzene-4,1-diyl))tetraphosphonic acid) (Scheme 1) was employed as the ligand and a Ag(I) phosphonate was successfully obtained under hydrothermal conditions. The cycloaddition of epoxides with CO2 to produce cyclic carbonates is one of the most promising ways for CO2 fixation,17–20 owing to it being an economical and green reaction. It is interesting that the compound exhibits high catalytic activity in the coupling of CO2 with epoxides. To the best of our knowledge, this is the first example of a Ag(I) phosphonate coordination polymer applied in CO2 chemical fixation.
IR: (KBr pellet, cm−1): 3422 (m), 3092 (w), 3044 (w), 1605 (s), 1535 (w), 1491 (m), 1418 (m), 1358 (s), 1327 (s), 1225 (m), 1130 (s), 1036 (S), 959 (m), 899 (m), 810 (s), 725 (w), 677 (s), 640 (w), 582 (w), 536 (m).
The loading of the catalyst is a 0.05% ratio based on the epoxide. After a given reaction time, a small amount of supernatant was taken out and used for Gas Chromatography (GC) analysis for calculating the conversion of the epoxide. At the end of the reaction, an aliquot of the reaction mixture was dissolved in CDCl3 and then filtered through a syringe filter (PTFE) for 1H NMR analyses. The product cyclic carbonate was confirmed by 1H NMR spectroscopy, and the yield was determined by GC and 1H NMR.
In a recycling experiment, the catalyst was isolated by centrifugation after the reaction, washed with dichloromethane three times and dried in air. The recovered catalyst was reused in the following reactions under the same conditions as those in the first run.
Fig. 1 A view of the 3D architecture of compound 1 in a ball–stick model (a) and the representation of the ⋯Ag–O–Ag⋯ chain (b). |
The stability test of the as-synthesized silver phosphonate was performed in different organic polar and nonpolar solvents for 24 h. PXRD patterns of the crystals after soaking in methanol, ethanol, dichloromethane, DMF (N,N′-dimethylformamide), acetonitrile and n-hexane solvents are in good agreement with the as-synthesized PXRD pattern (Fig. 2), suggesting the structural integrity of the silver phosphonate in solvent treatment.
The initial research employed epichlorohydrin as a model substrate to probe the optimized reaction conditions in the chemical conversion of CO2 into carbonates. The corresponding results and reaction conditions are listed in Table 1. The control experiments were carried out in the presence of n-Bu4NBr as a co-catalyst, referring to previous reports,24–30 with different reaction times. The representative amount of reactants is 20 mmol of epoxides and 0.3 mmol of co-catalyst n-Bu4NBr with a loading of 0.5 mol‰ ratio of silver phosphonate. When the reaction was performed under ambient conditions (entries 1–3 in Table 1), the yields were so low with 1.7%, 4.6% and 7.5% for 3 h, 6 h, and 12 h, respectively. Then, the CO2 pressure was increased to 1 MPa (entries 4–6 in Table 1); only a 17.8% yield was obtained even after 12 hours. When the temperature was gradually raised to 60 °C (entries 7–9 in Table 1) and 80 °C (entries 10–12 in Table 1), the yields were improved largely, with 65.8% and 94.3% for 12 hours, respectively. Afterwards, the temperature was increased to 100 °C, and the substrates were almost completely converted to cyclic carbonates after 6 h of reaction (entry 6), suggesting that temperature has a greater effect than pressure in such a reaction. Accordingly, the subsequent reactions were carried out at 100 °C under a 1 MPa CO2 reaction atmosphere, with n-Bu4NBr as the co-catalyst. Besides, AgNO3 was also employed as a catalyst for comparison (entry 15), and the yield was about 89.0%, which is a little lower than that obtained from compound 1 under similar conditions. The results manifest that the Lewis acid indeed can promote the coupling of CO2 with epoxides, as well as the superiority of silver phosphate. It is worth noting that AgNO3 as a homogeneous catalyst lacks recyclability.
Entry | T (°C) | P (MPa) | t (h) | Yied (%) |
---|---|---|---|---|
Reaction conditions: epichlorohydrin (20 mmol), catalyst (0.01 mmol) and n-Bu4NBr (0.3 mmol) under various conditions. Yields except for the final ones were calculated by GC using n-dodecane as an internal standard substance, and the final products and corresponding conversions were determined by 1H NMR spectroscopy. | ||||
1 | 25 | 0.1 | 3 | 1.7 |
2 | 25 | 0.1 | 6 | 4.6 |
3 | 25 | 0.1 | 12 | 7.5 |
4 | 25 | 1 | 3 | 5.9 |
5 | 25 | 1 | 6 | 9.8 |
6 | 25 | 1 | 12 | 17.8 |
7 | 60 | 1 | 3 | 20.9 |
8 | 60 | 1 | 6 | 50.3 |
9 | 60 | 1 | 12 | 65.8 |
10 | 80 | 1 | 3 | 68.9 |
11 | 80 | 1 | 6 | 90.6 |
12 | 80 | 1 | 12 | 94.3 |
13 | 100 | 1 | 3 | 93.6 |
14 | 100 | 1 | 6 | >99 |
15 | 100 | 1 | 3 | 89.3 |
To check the catalytic generality of the silver phosphonate, epoxide substrates with different sizes and functionalities were examined in the chemical fixation of CO2 into cyclic carbonates under the optimized conditions. The corresponding catalytic results are shown in Table 2. When the chlorine atom was substituted for a bromine atom, a slight increase was observed in the CO2 conversion with 95.6% within 3 hours, and also a complete conversion was observed within six hours. However, epoxybutane was converted to the corresponding cyclic carbonate with a lower conversion, 57.1%, 83.4%, 92.9%, and >99% for 3, 6, 9, and 12 hours, respectively. The above phenomena may be associated with the different electron-withdrawing or electron-donating substituents. Electron-withdrawing groups commonly facilitate nucleophilic attack during the ring opening of epoxides.28 The electronegativity order is –Br > –Cl > –CH3; as a consequence, the conversion of CO2 in the same amount of time is reduced in turn. When a larger sized epoxide, styrene oxide (SO), was employed, a lower decrease was observed in the product yields with 30.3%, 42.3%, 53.7% and 68.5% for 3, 6, 9, and 12 hours, respectively. The phenomenon in which the CO2 conversion decreases with the molecule size increase of epoxide substrates is consistent with most reports.28 When the phenyl group was substituted for a phenoxymethyl group, the reaction conversion was largely improved, with 83.0%, 90.2%, 96.4%, and >99% for 3, 6, 9, and 12 hours. Compared with SO, the higher yield for the allyl glycidyl is also attributed to the fact that the phenoxymethyl group is an electron-withdrawing substituent. The turnover number (TON) and turnover frequency (TOF) values according to the five kinds of epoxide substrates are also listed in Table 2. To better understand the activity of the silver phosphonate, comparisons with some MOF-based catalysts are listed in Tables S3 and S4,† in which epichlorohydrin and styrene oxide were chosen as the representative of small and large sized substrates, respectively. It was found that the TON and TOF values of the silver phosphonate for all the employed epoxides are even higher than those of some conventional porous MOF-based catalysts (Tables S3 and S4†). At the same time, in order to estimate the maximized conversion using the silver phosphonate catalyst, cycloaddition reactions were carried out using a larger amount of epichlorohydrin (40, 60, 100 mmol) and catalyst (0.01 mmol) under a constant pressure of 1 MPa (Table 2, entries 1a–1c) and at 100 °C. When the amount of epichlorohydrin is 100 mmol, the TON and TOF values are up to 8700 per mole of catalyst and 1450 per mole of catalyst per hour, proving that the silver phosphonate is a promising catalyst for the synthesis of cyclic carbonates from epoxides and CO2 for the chemical industry.
One crucial quality for heterogeneous catalysts is recyclability to evaluate their practical applications in industry. The reusability of the silver phosphonate was determined using epichlorohydrin as the reaction substrate. The reaction was performed under the optimized reaction conditions using 60 mmol epoxide and 0.01 mmol of catalyst for 6 h. After the reaction, the catalyst was centrifuged, washed three times with dichloromethane, and air-dried. The recovered catalyst was reused for subsequent reactions under the same conditions as those in the first run. After five cycles, there is no significant drop in the conversion, indicating that the catalytic activity of the silver phosphonate was still maintained. The powder X-ray diffraction (PXRD) pattern of the catalyst after five rounds was still in good agreement with that of the as-prepared one, showing structural integrity (Fig. 2). At the end of the reaction, the mixture filtrate was examined by inductively coupled plasma (ICP) analysis. No Ag leaching indicates the heterogeneous nature of the catalytic reaction. Besides, scanning electron microscopy (SEM) coupled with energy dispersive X-ray spectroscopy (EDS) was used to determine the morphologies and elemental composition of the samples before and after catalysis (Fig. 3), the results of which further proved the heterogeneous nature of the catalyst.
Based on previous reports,24–30 a plausible mechanism was proposed for the CO2 cycloaddition. As illustrated in Scheme S1,† firstly, the oxygen atom of the epoxide is activated by the metal centres and hydrogen bonding to initiate the epoxy ring. Then, Br− from n-Bu4NBr attacks the carbon atom of the activated epoxide, resulting in the epoxy ring opening. Subsequently, an epoxide intermediate is generated through the reaction between CO2 and the oxygen anion of the open ring. Finally, the ring closing leads to the final cyclic carbonate. At the same time, the catalyst is regenerated.
Footnotes |
† Electronic supplementary information (ESI) available: Crystallographic refinement details, additional tables and structural figures, PXRD and TG curves, and 1H NMR spectra. CCDC 2203855. For ESI and crystallographic data in CIF or other electronic format see DOI: https://doi.org/10.1039/d2ce01240e |
‡ These authors contributed equally. |
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