Yang
Hu‡
a,
Lihui
Zhang‡
a,
Zhuang
Wang
a,
Rongrong
Hu
*a and
Ben Zhong
Tang
*bc
aState Key Laboratory of Luminescent Materials and Devices, Guangdong Provincial Key Laboratory of Luminescence from Molecular Aggregates, South China University of Technology, Guangzhou 510640, China. E-mail: msrrhu@scut.edu.cn
bShenzhen Institute of Aggregate Science and Technology, School of Science and Engineering, The Chinese University of Hong Kong, Shenzhen, 2001 Longxiang Boulevard, Shenzhen City 518172, China. E-mail: tangbenz@cuhk.edu.cn
cAIE Institute, Guangzhou 510530, China
First published on 25th April 2023
Polythioamides with fascinating properties such as unique metal ion coordination ability, excellent thermal stability, good solubility, and high refractive index have attracted much attention recently, but their synthesis remains challenging, especially for aromatic polythioamides. In this work, multicomponent polymerizations of elemental sulfur, aromatic diamines, and aromatic dialdehydes with wide and economical sources were developed with the assistance of KOH. The polymerizations featured commercially available monomers with low cost, general applicability to various diamine and dialdehyde monomers, feasibility of large-scale synthesis, high atom economy, and no release of harmful byproducts, producing a series of aromatic polythioamides with high molecular weights of up to 54
700 g mol−1 and high yields of up to 96%. These polythioamides generally exhibited excellent thermal stability, good solubility, high thin film-light refractivity of 1.87 at 633 nm, and could be used for gold extraction. The MCP has provided an economical and efficient method to access unique aromatic polythioamides on a large scale, accelerating the exploration of sulfur-containing polymers as high-performance functional polymer materials.
Multicomponent polymerization (MCP) has been developed as a powerful method to concisely synthesize polymers from simple monomers, which have a series of advantages such as high efficiency, simple operation, mild conditions, high atom economy, and so on.12–14 Considering that elemental sulfur is an abundantly existing industrial byproduct whose profitable utilization is a global concern,15 a series of elemental sulfur-based multicomponent polymerizations were developed to directly convert elemental sulfur to sulfur-containing functional polymers such as polythioamides and polythioureas.2–4,16–20 For example, the MCP of sulfur, aliphatic diamines, and aromatic dialdehydes was first reported by Kanbara et al. to afford aliphatic polythioamides at 115 °C in DMAc;17,18 later, we reported a catalyst-free MCP of sulfur, aliphatic diamines, and aromatic diynes to produce seven aliphatic polythioamides with 100% atom economy at 100 °C in pyridine.4 A series of hyperbranched polythioamides with various topological structures, well-characterized chemical structures, and good solubility were also synthesized through these MCPs.19 Room temperature synthesis of polythioamides was also realized through this catalyst-free MCP with a pyridyl-activated diyne monomer.20 However, these catalyst-free sulfur-based MCPs were only applicable for aliphatic amine monomers, because the aromatic amines with weak alkalinity could not open the S8 ring to form reactive polysulfide anion species,2 which could hence only afford aliphatic polythioamides with non-conjugated flexible structures.
It is well-known that, compared with aliphatic polyamides, rigid aromatic polyamides possess superior thermal stability and mechanical properties, and are developed into high-performance engineering plastics,21 the development of aromatic polythioamides is hence desired to obtain advanced polymer materials. Recently, we have developed an MCP of sulfur, diamines, and benzyl diacids to synthesize aliphatic and aromatic polythioamides on a large scale through a decarboxylate process.2 It was found that through the assistance of K2CO3, less reactive aromatic diamine monomers could be included in this MCP to afford rigid aromatic polythioamides, with both sides of the thioamide moieties being directly linked to aromatic rings. However, commercially available benzyl diacids were limited, and it was crucial to develop new polymerizations with superior monomer choices in terms of cost, source, structural variations, and atom economy to realize economical and efficient synthesis of diverse aromatic polythioamides.
Considering that aromatic aldehydes have abundant natural sources, great structural diversity, low price, and are usually generated from biomass,22–24 in this work, we applied the inorganic base-assisted polymerization strategy to the MCP of sulfur, aromatic diamines and aromatic dialdehydes. In this reaction, elemental sulfur first underwent ring-opening reaction with the assistance of a base to form a polysulfide anion, which was then reacted with a Schiff base intermediate formed from an aldehyde and an amine, to furnish a thioamide product,18 and K2CO3 was reported to promote the aqueous phase reaction for the production of aromatic thioamides in water at 100 °C.25 Herein, an efficient KOH-assisted MCP of sulfur, aromatic diamines and aromatic dialdehydes was developed in organic solvent, affording various aromatic polythioamides with well-defined structures and high molecular weights (Mws) in high yields. Compared with previous synthetic approaches of aromatic polythioamides,2,7,9,26 more diversified polymer structures, lower cost, higher atom economy, scaled-up synthesis and no gas release were realized, demonstrating great potential in future large-scale preparation of these unique aromatic polythioamide materials.
:
[2a]
:
[5a] = 4.0
:
1.0
:
1.5 and monomer concentration [2a] = 0.4 M (Table S2†). Among all the tested polar solvents including pyridine, dimethylacetamide (DMAc), and dimethylformaldehyde (DMF), pyridine afforded the best polymerization result and polymer product with a Mw of 10
300 g mol−1 was obtained in 68% yield, suggesting that the alkalinity of pyridine may facilitate polymerization. Temperature was reported to be critical to the synthesis of polythioamides from sulfur-based MCPs.2,4 Similarly, in this polymerization, the polyimine intermediate formed from diamine and dialdehyde possessed poor solubility, which might cause its precipitation from the polymerization solution, hindering its further reaction with a polysulfide anion to produce thioamide moieties.17,18 Therefore, the polymerization temperature was fine-tuned from 90 to 115 °C, with a 5 °C interval to capture the sensitive influence of temperature on the MCP (Table S3†). Both the yield and Mw of the polymer product increased when the temperature was raised to 110 °C, and further heating to the boiling point of pyridine (115 °C) could cause a slight decrease in the yield and Mw. The monomer loading ratio was also crucial for the polymerization. An excess amount of dialdehyde was found to improve both yield and Mw, and when [2a]
:
[5a] = 1
:
2, a polymer with a Mw of 19
000 g mol−1 was obtained in 80% yield (Table S4,† entries 1–7). Considering the possible side reactions of aldehyde in the presence of KOH such as the Cannizaro reaction to consume aldehyde and result in stoichiometric imbalance of the amine and aldehyde, an excess amount of aldehyde in the MCP is beneficial for the polymerization. Moreover, when an excess amount of amine was adopted, only a low-molecular-weight product was afforded in low yield (Table S4,† entry 1). Similar to the reported sulfur-based MCPs,2,4,16 an excess amount of sulfur was also found to be beneficial for the polymerization, and the best result was obtained with the loading ratio of 1/8[S8]
:
[2a]
:
[5a] = 4.5
:
1.0
:
2.0, and a polymer with a Mw of 34
300 g mol−1 was furnished in 81% yield (Table S4,† entry 10).
In this polymerization, the inorganic base played a crucial role. Either weak bases such as Na2CO3, K2CO3, Cs2CO3, KF, and CsF, or a relatively dilute KOH (<0.4 M) aqueous solution could only afford an insoluble product, indicating that the reaction was probably stopped at the polyimine intermediate stage, which failed to convert to a polythioamide product. When [KOH] = 0.8 M and [2a] = 0.4 M, a satisfactory polymerization result was obtained; when [KOH] reached 1.2 M, only a low-molecular-weight product was generated (Table S4,† entry 13), due to the stoichiometric imbalance of the monomers caused by the aforementioned side reactions of the dialdehyde monomer and the potential degradation of these polythioamide structures at high temperature in the presence of a concentrated strong base. The monomer concentration was then optimized based on the loading ratio 1/8[S8]
:
[2a]
:
[5a]
:
[KOH] = 4.5
:
1.0
:
2.0
:
2.0. Increasing the monomer concentration was generally beneficial for the polymerization yield and Mw of the product, and the best result of a Mw of 41
700 g mol−1 and 87% yield was afforded when [2a] = 0.8 M (Table S5†). A further increase of the monomer concentration to 1.0 M caused gelation. Last but not least, the polymerization time was also optimized from 4 to 16 h. While elongation of the reaction time from 4 to 8 h could dramatically increase the yield and Mw to 94% and 54
700 g mol−1, respectively (Table S6†), further extension of the polymerization time to 16 h resulted in the reduction of both yield and Mw, suggesting a potential balance between polymerization and degradation of the polymer product at high temperature in the presence of a strong base with long reaction time.
Most importantly, with the three commercially available inexpensive monomers, the MCP of sulfur, 2a and 5a was conducted on a 50 mmol-scale under the above-mentioned optimal conditions, and 16.4 g of polymer product with a Mw of 19
600 g mol−1 was obtained in 91% yield, indicating the potential convenient and economical large-scale production of aromatic polythioamides (Table 1, entry 6).
Furthermore, the MCPs of sulfur, aromatic diamines and aromatic dialdehydes could be widely applicable to various aromatic amine and aldehyde monomers, which could afford diverse aromatic polythioamides. A series of commercially available, inexpensive aromatic diamines 2a–c and dialdehydes 5a–d were selected as the monomers (Table 2). In view of the different reactivity and solubility of each aromatic diamine and dialdehyde monomer, as well as their Schiff base intermediate, the polymerization conditions such as monomer concentrations, time, and loading ratio should be varied accordingly. The polymerizations generally proceeded well, affording polythioamides P2–P7 with satisfactory yields (up to 96%) and Mws (up to 25
300 g mol−1) (Fig. S2†). m-Phthalaldehyde 5a was found to produce polymers with higher Mws compared with those synthesized from p-phthalaldehyde 5b, probably owing to the improved solubility of the nonlinear-shaped polymer backbone with irregular intermolecular interactions. Besides, while the MCP of the relatively electron-rich aromatic dialdehyde 5c and electron-deficient aromatic dialdehyde 5d could proceed smoothly to afford polythioamides, the latter showed higher yield and Mw. It is worth mentioning that there were large numbers of commercially available, inexpensive aromatic dialdehydes, including those derived from biomass,22,23 to serve as monomers to tune the polymer backbone structures, which could greatly expand the aromatic polythioamide structure scope built from the previous MCPs of sulfur, aromatic diamines, and benzyl diacid monomers.2
| B | ||||||||
|---|---|---|---|---|---|---|---|---|
| Entry | Monomers | 1/8[S8] : [2a–c] : [5a–d] |
[2a–c] (M) | t (h) | Yield (%) |
M
w a (g mol−1) |
M
w/Mn a |
Solubility |
The reactions were carried out at 110 °C under nitrogen in pyridine and the yield was calculated based on the diamine monomers, [KOH] : [2a] = 2 : 1.a Mw and Mn were determined by GPC in DMF based on the polymethyl methacrylate standard samples.b Mw and Mn were determined by GPC with partially soluble polymers. √: the product is completely soluble, Δ: the product is partially soluble. |
||||||||
| P2 | 1 + 2b + 5a | 4.5 : 1.0 : 2.0 |
0.8 | 8 | 92 | 25 300 |
2.20 | √ |
| P3 | 1 + 2c + 5a | 4.5 : 1.0 : 2.0 |
0.5 | 12 | 93 | 14 200 |
1.67 | √ |
| P4 | 1 + 2a + 5b | 4.5 : 1.0 : 1.8 |
0.5 | 12 | 96 | 11 800 |
1.54 | Δ |
| P5 | 1 + 2b + 5b | 4.5 : 1.0 : 1.8 |
0.4 | 12 | 88 | 9100 | 1.33 | Δ |
| P6 | 1 + 2a + 5c | 4.5 : 1.0 : 1.5 |
0.5 | 12 | 42 | 5900 | 1.20 | √ |
| P7 | 1 + 2a + 5d | 4.5 : 1.0 : 1.8 |
0.5 | 12 | 69 | 14 800 |
1.48 | √ |
S carbon peak of the thioamide group in P1 at δ 196.33 (Fig. S4†), and similar characteristics of HN–C
S carbon resonance were also observed at δ 189.13–196.51 in the 13C NMR spectra of P2–P7 (Fig. S5†). The FT-IR spectra of P1–P7 were also similar to that of model compound 4 (Fig. S6 and S7†).
![]() | ||
| Fig. 2 1H NMR spectra of (A) 2a, (B) 3, (C) 5a, (D) 4, and (E) P1 in DMSO-d6. The solvent peaks are marked with asterisks. | ||
Furthermore, the existence of sulfur in these aromatic polythioamides was confirmed by X-ray photoelectron spectroscopy (XPS), and the binding energies of S 2p were observed at 162.20–163.81, which overlapped with those of model compound 4, but were not in the range of elemental sulfur, suggesting that the existing form of the sulfur atom in these polymers was indeed thioamide (Fig. S8†).
Moreover, thermogravimetric analysis (TGA) suggested that these aromatic polythioamides possessed high thermal resistance with their decomposition temperatures at 5 wt% weight loss ranging from 295 to 363 °C, and high char yields of 50–67% at 800 °C, owing to their strong intermolecular and intramolecular interactions including hydrogen bonds among the abundant thioamide moieties and π–π stacking interactions among the large number of aromatic rings (Fig. 3). Their crystallinity was also studied by powder XRD, and diffraction peaks of P5 were observed (Fig. S9†), suggesting that the linear-shaped polymer backbone was beneficial for its regular alignment and packing.
Different polythioamides P1–P7 were then utilized for gold extraction, using different amounts of solid powder (Fig. 4 and Table S7†). P7, prepared from 2,6-pyridinedicarboxaldehyde, showed the best performance among these polymers and its extraction capacity was 788 mg Au3+ g−1 calculated from the extraction efficiency obtained with 1 mg polymer to extract Au3+ from an aqueous solution with [Au3+]0 = 100 mg L−1, which showed higher efficiency and capacity with the best polythioamides in the literature.2 The pyridine moieties in P7 might also serve as a metal coordination ligand to extract Au3+, together with thioamide moieties, to improve the gold extraction performance.
![]() | ||
| Fig. 4 The extraction efficiency of Au3+ with different amounts of solid powder of aromatic polythioamides P1–P7. [Au3+]0 = 100 mg L−1. VAu3+ = 10 mL. | ||
Footnotes |
| † Electronic supplementary information (ESI) available: Materials and instruments, synthetic procedures and characterization data; single crystal data and MS spectrum of 4; effect of solvent, temperature, monomer loading ratio, base and monomer concentrations, polymerization time, and monomer structures on the MCP; GPC curves of P1–P7; 1H, 13C NMR and FT-IR spectra of P1–P7 and model compound; XPS spectra and XRD patterns of the polythioamides; selectivity test and effect of polymer dosages about gold extraction. CCDC 2225162. For ESI and crystallographic data in CIF or other electronic format, see DOI: https://doi.org/10.1039/d2py01560a |
| ‡ These authors have equally contributed to this work. |
| This journal is © The Royal Society of Chemistry 2023 |