Bifunctional chlorhexidine-based covalent organic polymers for CO2 capture and conversion without a co-catalyst

Ruiying Zhang ab, Yue Shen b, Lin Liu *a and Zhengbo Han *a
aCollege of Chemistry, Liaoning University, Shenyang 110036, P. R. China. E-mail: ceshzb@lnu.edu.cn; liulin@lnu.edu.cn
bCollege of Science, Northeastern University, Shenyang 110819, Liaoning, P. R. China

Received 29th September 2024 , Accepted 19th November 2024

First published on 3rd December 2024


Abstract

Two new cobalt/zinc-coordinated bifunctional covalent organic polymers (COP-Co and COP-Zn) based on chlorhexidine are prepared as heterogeneous catalysts for carbon dioxide (CO2) conversion. Due to the Cl nucleophile and cobalt/zinc Lewis acid sites, COP-Co and COP-Zn can efficiently convert CO2 and epoxides into cyclic carbonates under mild conditions without a co-catalyst.


Carbon dioxide (CO2) is accumulating in the atmosphere, causing many global greenhouse effect problems; hence, slowing the current trend of global warming needs to be addressed.1 Mounting attention has been given to converting CO2 into high value-added products.2 Among diverse CO2 conversion technologies, the cyclic carbonates formed by cycloaddition of CO2 with epoxides are high-value fine chemical intermediates and are indispensable for both the pharmaceutical and organic synthesis industries.3 Traditional homogeneous catalysts such as halogen ionic liquids and metal complexes have played a dominant role in this reaction.4 However, these homogeneous catalysts are faced with difficulties in the recovery of the catalyst and purification of the product, thus increasing the cost.5 In contrast, heterogeneous catalysts with structural and thermal stability are beneficial for recyclability.6 Nevertheless, harsh reaction conditions such as high pressure and temperature obstruct factory needs in large-scale production. Hence, considerable efforts have been made to search for suitable catalysts for CO2 conversion.

Porous materials such as metal–organic frameworks and covalent organic frameworks have been extensively developed as typical heterogeneous catalysts for CO2 conversion owing to their large surface area, high porosities, and good stability.7 Among them, covalent organic polymers (COPs) have emerged as promising candidates for applications owing to their high porosity, fast kinetics, and designable pore structure.8 Several metal ions such as Zn, Co, Al, and Cu have been introduced into COP networks to provide a wide variety of metal-functionalized COPs.6,9 Due to the porous structures and the Lewis acid sites of the incorporated metal moieties, the adsorption capacity and the catalytic performance of these COPs can be significantly enhanced. For example, Deng et al. reported a Zn-based COP catalyst for efficient CO2 cycloaddition.10 Chen et al. developed a series of aluminum porphyrin-based COPs, which are considered excellent catalysts for converting CO2 into cyclic carbonates.11 Consequently, great success encouraged researchers to seek COP materials for CO2 capture and applications.

Chlorhexidine (CHX) with abundant neutral tetradentate donors and chlorines in the skeleton exhibits excellent coordination ability for many metal ions. Moreover, Cl is regarded as the nucleophile in catalytic reactions. Generally, the exploration of chlorhexidine has focused on clinical antimicrobial research but has rarely been used in the synthesis of COPs. For instance, three new chlorhexidine complexes synthesized from copper chloride, copper bromide, and acetate indicate that chlorhexidine and copper salt has a quadrilateral twisted octahedral symmetry with a ratio of 1[thin space (1/6-em)]:[thin space (1/6-em)]1.12 Therefore, chlorhexidine has been identified as a prospective candidate for developing COP catalysts.

Herein, two new metal-functionalized COPs (COP-Co and COP-Zn) are synthesized using CHX-Co/Zn complexes (CHX = chlorhexidine) and nitrogen-rich tri(1H-imidazole-1-yl)-1,3,5-triazine (TIT) under solvothermal conditions (Fig. 1). Due to the synergistic effects of Co/Zn Lewis acid sites and Cl nucleophile, the COP-Co and COP-Zn catalysts can capture and convert CO2 under mild conditions in the absence of a co-catalyst.


image file: d4cc05095a-f1.tif
Fig. 1 Synthesis route of COP-M (M = Co, Zn).

The morphological structures of COP-Co and COP-Zn were analyzed by scanning electron microscopy (SEM) and transmission electron microscopy (TEM). Fig. 2a and b show that COP-Co is composed of relatively uniform nanoparticles with a size of 200 nm and possess a porous structure, which can facilitate epoxide penetration and fast reaction kinetics. The element mappings of COP-Co further show that C, N, Cl, and Co elements are uniformly distributed in the skeleton (Fig. 2c and Fig. S1, ESI). Fig. 2d shows that COP-Zn consists of densely packed nanoparticles. The TEM image of COP-Zn demonstrates a remarkably aggregated nanoparticle structure (Fig. 2e). Additionally, the elemental mappings of COP-Zn illustrate the homogeneous distribution of C, N, Cl, and Zn elements in the COP-Zn framework (Fig. 2f and Fig. S2, ESI).


image file: d4cc05095a-f2.tif
Fig. 2 (a) SEM image, (b) TEM image, and (c) element mappings of COP-Co. (d) SEM image, (e) TEM image, and (f) element mappings of COP-Zn. (g) FT-IR spectra of TIT, CHX, CHX-Co, COP-Co, CHX-Zn, and COP-Zn. (h) Solid-state 13C-NMR spectrum of COP-Zn. (i) High-resolution N 1s and (j) Cl 2p XPS spectra of COP-Zn and COP-Co.

The broad peaks were observed in X-ray diffraction patterns, proving the amorphous states of COP-Co and COP-Zn (Fig. S3, ESI). This is caused by the disordered accumulation of polymers during the formation process. The Fourier transform infrared (FTIR) spectra were carried out to certify the structures of COP-Co and COP-Zn (Fig. 2g). The peak at 602 cm−1 of CHX-Co and CHX-Zn related to the formation of Co/Zn–N bonds. The vibration peak at 1250 cm−1 belonging to C–Cl groups of CHX disappears, confirming the formation of COP-Co and COP-Zn. Furthermore, the molecular structure of COP-Zn was further illustrated by the solid-phase 13C-NMR spectra (Fig. 2h). The peak at 160.3 ppm is assigned to the triazine ring carbon. The peak at 33.3 ppm is derived from–C–N groups, while the other two lower intensity peaks at 25.9 and 29.4 ppm are ascribed to sp-hybridized –CH carbons in the CHX moiety. The peak at 142.6 ppm corresponded to the aromatic ring carbon shifts to 125.3 ppm in COP-Zn, indicating that CHX-Zn is connected to imidazole to produce imidazolium.13 The molecular weight and polydispersity index of COP-Co tested by gel permeation chromatography are 18[thin space (1/6-em)]841 g mol−1 and 2.05, respectively.

The chemical compositions of the samples were examined by X-ray photoelectron spectra (XPS) tests with Ar ion etching 50 nm deep. The atomic compositions of Co and Zn are determined to be 7.0 wt% and 7.5 wt%, respectively. Several peaks of COP-Zn located at around 202, 285, 400, and 1035 eV can be ascribed to Cl 2p, C 1s, N 1s, and Zn 2p, respectively (Fig. S4, ESI). The peaks of COP-Co located at 202, 285, 100, and 800 eV belong to Cl 2p, C 1s, N 1s, and Co 2p, respectively (Fig. S5, ESI). The C 1s spectra of COP-Co and COP-Zn exhibit three peaks at 288.9, 286.3, and 284.8 eV, which are ascribed to –C[double bond, length as m-dash]N, C–N, and –C[double bond, length as m-dash]C/C–C groups, respectively (Fig. S6, ESI).14 The N 1s spectra of COP-Co and COP-Zn are decomposed into four peaks: 400.5, 399.9, 399.2, and 398.2 eV, which are related to C–N+, C–N, C[double bond, length as m-dash]N, and N–Co/Zn units, respectively (Fig. 2i).15 Additionally, the N 1s spectra of CHX, CHX-Co, and CHX-Zn are explored. In contrast with CHX, the peaks that appeared at around 455.6 eV belong to N–Zn and N–Co metal bonds, indicating the formation of CHX-Co/Zn (Fig. S7, ESI). The Cl 2p peaks of COP-Co and COP-Zn that appeared at 198.9 eV and 197.3 eV are ascribed to chloride Cl, relating to the formation of COP-Co and COP-Zn (Fig. 2j). Compared to COP-Co and COP-Zn, the Cl 2p peaks of CHX, CHX-Co, and CHX-Zn located at 200.3 eV and 201.9 eV correspond to organic Cl (Fig. S8, ESI). This result proves that CHX-Co/Zn is associated with TIT and the organic Cl is converted into a chloride Cl.16 The peaks of Zn 2p located at 1023 eV and 1046 eV correspond to Zn 2p3/2 and Zn 2p1/2, respectively (Fig. S9, ESI). The peaks of the Co 2p spectra appearing at 784 eV and 801 eV are associated with Co 2p3/2 and Co 2p1/2, respectively. Both peaks are accompanied by satellite peaks at 789 eV and 805 eV (Fig. S10, ESI). The thermogravimetric analysis results indicate that COP-Co and COP-Zn could be stable up to 210 °C and 222 °C, respectively, indicating their good thermal stability. The glass transition points of COP-Co detected by differential scanning calorimeter are 155 °C (Fig. S11, ESI).

The surface areas and the porous structures of COP-Co and COP-Zn were investigated by N2 and CO2 adsorption/desorption tests. The Brunauer–Emmett–Teller (BET) surface area of COP-Co is 136 m2 g−1. COP-Co exhibits both type-I and type-IV behaviors, indicating that COP-Co is composed of micropores and mesopores (Fig. S12, ESI).12 The pore size of COP-Co characterized using non-local density functional theory is 0.7 and 3.8 nm. Due to the degradation and agglomeration of the frameworks, the COP-Zn exhibits a type-IV curve with an H3-type hysteresis ring and a much lower BET surface area (47 m2 g−1) than COP-Co. The median pore size of COP-Zn calculated by the Barrett–Joyner–Halenda method is in the range of 2.6–3.5 nm (Fig. S13, ESI). The chemical adsorption abilities of CO2 and the possible reaction mechanisms of COP-Co/COP-Zn are characterized by the Langmuir model based on eqn (S1) (ESI) (Fig. S14, ESI).14 The Langmuir surface areas of COP-Co and COP-Zn are 211 m2 g−1 and 79 m2 g−1, respectively. At 273 K, COP-Co and COP-Zn display CO2 adsorption capacity of 57.3 mg g−1 and 27.6 mg g−1, respectively. At 298 K, the CO2 adsorption capacities of COP-Co and COP-Zn are 31.2 mg g−1 and 22.5 mg g−1 (Table S1, ESI). These results verify that CO2 capture could be based on chemical absorption. The strong CO2 capture abilities are attributed to the large surface area.

Based on the above results, the attractive structures and high CO2 adsorption capacities endow COP-Co and COP-Zn as potential catalysts for the cycloaddition of CO2 and epoxides to form cyclic carbonates. The reactions were purged to 1.0 MPa pressure under co-catalyst-free conditions. The products were obtained by removing the COP-Co and COP-Zn from the reaction system through centrifugation. The conversion was determined by eqn (S2) (ESI) and gas chromatography (Fig. S15, ESI). To investigate the systematic optimization of reaction parameters such as reaction temperature, catalyst amount, and reaction time, typical reactions were conducted using propylene oxide (PO) substrate and CO2. When the weight of COP-Co was 30 mg, 40 mg, 50 mg, and 60 mg, the PO conversions were 17.3%, 40.8%, 46.3%, and 46.8%, respectively (Table 1, entries 1–4). The conversion increases according to the amount of COP-Co; that is, the concentration of the catalytic active site determines the catalytic efficiency. When the temperature increases from 80 °C to 90 °C, the conversion of PO advances from 46.8% to 49% (Table 1, entry 5). However, when the reaction temperature rises from 90 °C to 100 °C, the conversion increases almost negligibly (Table 1, entry 6). These results verify that 90 °C is the optimal temperature. When the reaction times are 3, 6, 9, and 12 hours, the conversions are 50.7%, 59%, 80.2%, and 98.4%, respectively (Table 1, entries 6–9). Observably, the optimized reaction conditions (50 mg catalyst, 90 °C, 12 hours, 1 MPa) are obtained and applied to the subsequent catalytic reactions. Moreover, the epoxides with different sizes were investigated under the optimized conditions (Table 1, entries 9–18). All of the substrates are effectively converted into their corresponding cyclic carbonates. When COP-Co is used as a catalyst, the conversion of PO is 98.4% with a turnover number (TON) value of 164 while the COP-Zn catalyst represents a conversion of 90.2% with a TON value of 150. Compared with the reported catalysts, COP-Co and COP-Zn show good catalytic performance for CO2 cycloaddition under co-catalyst-free conditions (Table S2, ESI). Both COP-Co and COP-Zn catalysts exhibit a certain size selection effect. With the substrate molecular size increasing, the conversions of epoxides obviously decrease.17

Table 1 Cycloaddition of CO2 and different epoxides catalyzed by COP-Co and COP-Zn in the absence of a co-catalyst

image file: d4cc05095a-u1.tif

Entry R Amount (mg) Time (h) Conversiona (%) TONb
a Conversions were determined by gas chromatography. b TON = (mole of products)/(mole of active sites). Reaction conditions: epoxides (10 mmol), CO2 (1 MPa). Catalyst. c COP-Co. d COP-Zn. Temperature. e 80 °C. f 90 °C. g 100 °C.
1ce Me 30 3 17.3 24
2ce Me 40 3 40.8 85
3ce Me 50 3 46.3 77
4ce Me 60 3 46.8 65
5ce Me 50 3 49.0 82
6cg Me 50 3 50.7 85
7cf Me 50 6 59.0 98
8cf Me 50 9 80.2 131
9cf Me 50 12 98.4 164
10df Me 50 12 90.2 150
11cf CH2Cl 50 12 93.1 155
12df CH2Cl 50 12 87.7 146
13cf Et 50 12 83.0 138
14df Et 50 12 55.4 92
15cf Ph 50 12 53.1 89
16df Ph 50 12 20.6 34
17cf C4H9OCH2 50 12 40.0 67
18df C4H9OCH2 50 12 16.9 28


For heterogeneous catalysts, the recyclability is an important factor to evaluate catalytic performance. To probe the recyclability of COP-Co and COP-Zn, cycling reactions were performed using PO as the substrate under optimized conditions. The COP-Co and COP-Zn catalysts were recovered and reused by centrifugation, washing, and drying for multiple cycles (Fig. S16, ESI). The conversion of the COP-Co catalyst decreases slightly from 98.4% to 85.1% after 5 cycles at a relatively mild CO2 pressure (1 MPa) and temperature (90 °C), demonstrating the recyclability and stability of COP-Co. Unfortunately, the cycling stability of COP-Zn is relatively poor. After five cycles of COP-Zn, the PO conversion decreases from 90.2% to 80.5%. This is due to the fact that trace amounts of water in the catalytic reaction system form inactive zinc species, resulting in the destruction of the reactivity.18 After five cycles, the morphology of the COP-Co and COP-Zn catalysts remains nearly unchanged, illustrating the remarkable structural stability (Fig. S17, ESI). Leaching tests were carried out to verify the heterogeneous properties of the COP-Co and COP-Zn catalysts. When the catalysts are removed from the reaction systems, the increase of conversion is negligible, proving that COP-Co and COP-Zn are heterogeneous catalysts (Fig. S18, ESI).

Based on the current research results,19 the possible reaction mechanism of COP-Co for the cycloaddition reaction of CO2 with epoxides is proposed (Fig. 3). Firstly, oxygen atoms in the epoxides are coordinated to metal Lewis acid sites (Co2+ for COP-Co) to form a powerful electron-rich intermediate that can activate the epoxide ring. Meanwhile, Cl ions attack the C–O bond with less steric hindrance in epoxides, leading to the ring-opening reaction. Then, the CO2 enriched in the COP-Co and COP-Zn catalysts interacts with the ring-opening epoxides to generate alkoxy anions.20 Furthermore, the N-rich framework of COP-Co can increase the adsorption of CO2, thus improving the CO2 capture ability and accelerating the reaction. Finally, the alkoxy anion closes its ring to form cyclic carbonate and COP-Co is regenerated.


image file: d4cc05095a-f3.tif
Fig. 3 Proposed catalysis process of COP-Co for CO2 conversion.

In conclusion, two new bifunctional cationic COP-Co and COP-Zn based on CHX are prepared as the heterogeneous catalysts for CO2 conversion. Both COP-Co and COP-Zn present high BET surface area and good CO2 adsorption capacity. The COP-Co and COP-Zn exhibit certain size selection effects as heterogeneous catalysts for CO2 cycloaddition reaction. The Cl acts as a nucleophile to facilitate the ring-opening of epoxides and cobalt/zinc act as Lewis acid centers. Due to the synergistic effects, the COP-Co and COP-Zn can efficiently convert CO2 and epoxides into cyclic carbonates with high conversion, durability, and recyclability under relatively mild conditions in the absence of a co-catalyst. This work expands the categories of COPs for future applications and provides a new way to capture and transform CO2. Meanwhile, due to the limitations of open-air implementation, these COPs for CO2 capture from laboratory to industrial applications still require in-depth exploration.

The authors kindly acknowledge financial support from the National Natural Science Foundation of China (22171121), Applied Basic Research Plan of Liaoning Province (2023JH2/101300007), the Chey Institute for Advanced Studies' International Scholar Exchange Fellowship for the academic year of 2023–2024, and the Fundamental Research Funds for Public Universities in Liaoning.

Data availability

The data supporting this article have been included as part of the ESI.

Conflicts of interest

There are no conflicts to declare.

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Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4cc05095a

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