Open Access Article
Huili Wanga,
Tiansheng Wangab,
Murielle Berlandea,
Ahmed Subrati
c,
Sergio Moya
c,
Lionel Salmon
b,
Nathalie Darod,
Nathalie Audebrande,
Jean-René Hamon
e,
Haizhu Yu*f,
Jean-Luc Pozzo
*a and
Didier Astruc
*a
aUniversité de Bordeaux, ISM, UMR CNRS No. 5255, 33405 Talence Cedex, France
bUniversité de Toulouse, LCC, UPR CNRS No. 8241, 31077 Toulouse Cedex, France
cSoft Matter Nanotechnology Lab, CIC biomaGUNE, Paseo Miramón, 182, 20014 Donostia-San Sebastián, Gipuzkoa, Spain
dUniversité de Bordeaux, CNRS, Bordeaux INP, ICMCB, UMR No 5026, 33600 Pessac, France
eUniv Rennes, ISCR (Institut des Sciences Chimiques de Rennes), UMR 6226, F-35000 Rennes, France
fDepartment of Chemistry and Center for Atomic Engineering of Advanced Materials, Anhui Province Key Laboratory of Chemistry for Inorganic/Organic Hybrid Functionalized Materials, Anhui University, Hefei, Anhui, 230601 People's Republic of China
First published on 3rd February 2026
The catalytic activation of CO2 under mild conditions to form value-added heterocyclic products is of paramount interest. Copper sulfides are a large class of materials, many of which are found as minerals in nature. They often show remarkable physical properties, and further studies of their catalytic properties need to be conducted. The simple compound Cu2S was designed, its synthesis was improved, and its catalytic activities in CO2 activation are disclosed here. Synthesized Cu2S is shown to be an efficient heterogeneous catalyst for the carboxylation of propargylamines under ambient temperature and pressure conditions and the carboxylation of terminal alkynes under one atm CO2 at 80 °C. CO2 is transformed into high-value-added chemicals with a wide range of substrates with excellent yields, and the catalyst is easily reused at least 5 times without significant activity reduction. The catalytic and recycling performances are significantly better for synthesized Cu2S compared to those of its commercial analogue. In summary, Cu2S is a new catalyst that is simple, non-toxic, self-supported, recyclable, and practical. These findings open a general route to the catalytic properties of Cu2S toward, not only mild CO2 activation applications, but also a variety of other useful reactions.
Most of the known catalysts for carboxylation reactions are based on noble metals,14,15 but, in order to achieve widespread application, the use of such expensive and rare noble metals should as much as possible be avoided.16–18 In recent years, researchers have explored the application of various catalysts with propargylamines and in other carboxylation reactions.19–23 For example, Qiao24 developed a Cu6–NH2 nanocluster with a distorted octahedral Cu6 core and NH2-functionalized ligands, which catalyzes the cyclization of propargylamines with CO2 under mild conditions. Cu6–NH2 exhibits good catalytic activity, due to its accessible active sites. The nanocluster also exhibits excellent stability, good recrystallization, and reusability, with no significant decrease in catalytic performance over five catalytic cycles. However, there are problems such as complex synthesis process and possible reaction of NH2 sites with impurities. Kong25 developed a long-term stable copper catalyst coordinated with sugar acetate (acetylglucose) and 2-methylimidazoline. This catalyst has multiple active sites, enabling it to efficiently capture and simultaneously activate CO2 and propargylamines. Its turnover frequency is as high as 880 h−1, which is about 180 times that of CuCl2, and the catalytic activity of Im–Cu A did not decrease after 20 repeated reactions. However, there is a potential problem of uneven distribution of active sites.26–28 Qiu29 proposed an efficient and stable CuI-anchored porous covalent organic framework CuI@TpBD-COF, in which TpBD is a β-ketoamine with carbonyl and amine group (–NH2, –NHR or –NR2), with these two groups separated by two carbon atoms. This organic framework is used to effectively catalyze the carboxylic cyclization reaction of propargylamines with CO2 and to synthesize various functionalized oxazolidinone derivatives under mild conditions with yields of up to 99% and a turnover frequency (TOF) of 1058 h−1. In addition, when simulated flue gas was used as the CO2 source, CuI@TpBD-COF also showed good catalytic activity. However, the synthesis cost of COF materials is high.30–32 Gu33 loaded nano-Cu2O on a ZIF-8 support to prepare Cu2O@ZIF-8 catalyst, which can effectively catalyze the cyclization of propargylalcohols and propargylamines with CO2 to produce valuable α-alkylene cyclic carbonates and oxazolidinones, with turnover number (TON) values of 12.1 and 19.6, respectively, and this catalyst was recycled at least 5 times. However, Cu2O is toxic, and its TON is low.34–36
Despite the performances of these Cu-based systems in the cyclization of propargylamines with CO2, these catalysts often suffer from structural complexity, high synthesis costs, toxicity issues (e.g., Cu2O), instability under ambient conditions, and limited scalability.37–40 To address these challenges, we have developed a Cu2S catalyst that offers a promising alternative. Cu2S is a low-cost, environmentally friendly, structurally stable, and easy to synthesize material under mild conditions. More importantly, it provides easily accessible active sites, exhibiting high catalytic efficiency and recyclability in the cyclization of propargylamines with CO2 even under mild conditions. This work highlights the role of Cu2S as a powerful and sustainable copper-based catalyst platform for green CO2 conversion chemistry. The synthesis and their effectiveness in promoting this environmentally beneficial transformation will be discussed. By harnessing the potential of such a catalyst system, this approach represents a significant step forward in the utilization of CO2 as a valuable chemical feedstock.
To investigate the valence state of copper in the present catalyst, which is crucial for the rationalization and understanding of the catalytic activity,44–48 XPS measurements were performed, and the results are shown in Fig. 2. The Cu 2p XPS of synthesized Cu2S both before and after the catalytic carboxylation reaction, as presented in Fig. 2(a) and (b), respectively, show two spin–orbit doublets with Cu 2p3/2 components at 932.4 eV (bulk monovalent Cu) and 933.2 eV (surface monovalent Cu), which indicate that Cu in the synthesized Cu2S exclusively exists in the form of Cu(I).49–52 Emergence of the surface Cu(I) is ascribed to the presence of surface-confined Cu-deficient Cu2S domains wherein Cu–S covalency is weakened. The XPS data also obtained after the catalytic carboxylation reaction show that copper remains in the Cu(I) state. However, for commercial Cu2S (Fig. 2c and d), it was found that, in addition to the two bands around 932.5 eV and 952.4 eV for Cu(I), there were also two discernible Cu 2p spin–orbit doublets indicating the presence of Cu(0) and Cu(II) after catalysis. Therefore, the XPS results thoroughly demonstrate that the synthesized Cu2S has a high Cu(I) purity, including after recovery from the catalytic reaction, while having a good recycling performance. The Cu XPS analysis results are summarized in Table S1.
Fig. S1(a) shows the valence band XPS of synthesized and commercially available Cu2S before and after catalysis. Only the profiles of synthesized Cu2S and recycled synthesized Cu2S resemble the profile of the reference Cu2S.53 Fig. S1(b) shows the Auger signals for Cu, Cu LMM. Table S2 lists the Auger parameters of synthesized and commercially available Cu2S before and after catalysis. Analysis of this parameter and inspection of peak shapes allow for assignment of copper species.54 The synthesized Cu2S and recycled synthesized Cu2S respectively retained Auger parameters of 1849.93 eV and 1849.96 eV, values that are consistent with the reference Cu2S with its Auger parameter of 1849.84 eV,54 indicating that Cu is in the monovalent state, Cu(I), in the synthesized Cu2S and recycled synthesized Cu2S. However, the other entries reveal values that differ from that of Cu2S. To demonstrate the chemical state similarities between the reference Cu2S and synthesized Cu2S of this work, a Cu 2p3/2 vs. Cu LMM Wagner (chemical state) plot is presented in Fig. S1(c). Only synthesized Cu2S and recycled synthesized Cu2S fall within the vicinity of the reference Cu2S and along the diagonal line corresponding to the constant Auger parameter of 1850 eV. This confirms the sole presence of Cu(I) in synthesized Cu2S and recycled synthesized Cu2S. The shift of positions along the 1850 eV diagonal line can be attributed to changes in local charge density, particularly in the case of recycled synthesized Cu2S due to presence of some nitrogen species with total atomic content of 3.15%. Another crucial difference is revealed from the analysis of the S 2p XPS, as shown in Fig. S2 and summarized in Table S3. The synthesized Cu2S before and after catalysis retains a much larger proportion of lattice S compared to S oxide. The contrary situation is observed in the case of commercial Cu2S before and after catalysis, where the majority of S is in the form of S oxide. Furthermore, from the S 2p XPS analysis of synthesized Cu2S and recycled synthesized Cu2S, we were able to probe two lattice S 2p spin–orbit doublets, corresponding to bulk and surface lattice sulfides. The bulk sulfide components have characteristically smaller full-width at half maximum (FWHM) and binding energy values when compared to the surface sulfide components. The bulk lattice sulfide exists within more crystalline domains, with higher electron delocalization, stronger Cu–S covalency, and stronger electron (back-)donation due to the higher coordination state of sulfur in the bulk as compared to the lower coordination state of sulfur in surface-bound Cu-deficient Cu2S. It is important to note that the bulk lattice sulfide contribution increases by 10.3 atomic%, while the surface lattice sulfide contribution decreases by 7.2 atomic% after recycling the synthesized catalyst. In addition, the Cu(I) bulk contribution increases by 16.3 atomic%, while the Cu(I) surface contribution decreases by 16.3 atomic% after recycling the synthesized catalyst. This indicates that the catalytic and recycling processes diminish the surface Cu-deficient layer bringing the catalyst closer to the stoichiometric Cu-to-S atomic ratio (Cu/S) of 2 (note the Cu/S values in Table S2). This can also serve as an explanation for the shift of recycled synthesized Cu2S along the 1850 eV Auger parameter diagonal line shown in Fig. S1(c). The collective analysis of the Auger signal, valence band, and sulfur chemical environment, indicates that commercial Cu2S is more susceptible to ambient oxidation and hydrolysis, both before and after catalysis, than the synthesized Cu2S.
Fig. 3 shows the (HR-)TEM/STEM/EDS results of the synthesized Cu2S. The sample exhibits a strong tendency to aggregate as observed in Fig. 3(a and b). Characteristic Cu2S diffraction signals arising from distinct lattice planes were probed by HR-TEM as demonstrated in Fig. 3(c–h).55 Cu2S is prone to surface oxidation/contamination and this is evidenced by the presence of an ∼2.3 nm amorphous layer covering crystalline grains/cores, as seen in Fig. 3(g). The STEM image shown in Fig. 3(i) reveals an aggregate of synthesized Cu2S and EDS elemental maps of Cu and S are presented in Fig. 3(j and k). The elemental mapping shows uniform distribution of Cu and S in the sample. Values of Cu/S are seen to fluctuate between 1.9 and 2.0 averaging to 1.93 as determined from the EDS line scan, shown in Fig. 3(l). This supports the XPS findings by confirming the presence of a surface Cu-deficient Cu2S layer.
The oxazolidinones obtained from the chemical transformation of propargylamines and CO2 are important intermediates in the syntheses of heterocyclic compounds in organic chemistry and in the development of antibacterial drugs in medicinal chemistry.56 Therefore, the potential application of Cu2S in the catalytic cyclizing carboxylation of propargylamine with CO2 was explored.24,29 To optimize catalytic conditions, N-2-propyn-1-ylbenzylamine was initially selected as a model substrate (Table 1). The heterogeneous reaction with this substrate proceeded smoothly at room temperature (25 ± 1 °C) in the absence of a cocatalyst, yielding the target product, 3-benzyl-5-methylene-2-oxazolidinone, in 99% yield within 8 hours (Table 1, entry 1). Substituting TEA or cesium carbonate as the base for DBU reduced the yield to trace amounts and 50%, respectively (Table 1, entries 2 and 3). Changing the solvent from CH3CN to DMF, CH3OH, or DMSO reduced the yield to 80%, 50%, and 30%, respectively (Table 1, entries 4, 5, and 6). Shortening the reaction time to 4 hours reduced the yield to 78% (Table 1, entry 7). Changing the substrate dosage from 0.5 mmol to 0.1 mmol and 1 mmol, respectively, yields reached 98% and 90%, respectively (Table 1, entries 8 and 9). In the absence of catalyst or base, no target product was produced (Table 1, entries 10 and 11). Subsequently, under the same catalytic conditions, commercially available Cu2S was used as the catalyst, achieving a product yield of 80% (Table 1, entry 12). The results demonstrate that the synthesized Cu2S is a highly efficient catalyst for the carboxylation of propargylamine with CO2 at room temperature and under atmospheric pressure without the need for a cocatalyst.
| Entry | Catalyst | Substrate (mmol) | Base | Solvent | t (h) | Yieldb (%) |
|---|---|---|---|---|---|---|
| a Reaction conditions: N-benzylprop-2-yn-1-amine (0.5 mmol), Cu2S (0.005 mmol), DBU (0.5 mmol), CH3CN (3 mL), CO2 (balloon), room temperature.b The yields were determined by 1H NMR analysis using mesitylene as the internal reference. | ||||||
| 1 | Cu2S | 0.5 | DBU | CH3CN | 8 | 99 |
| 2 | Cu2S | 0.5 | TEA | CH3CN | 8 | Trace |
| 3 | Cu2S | 0.5 | Cs2CO3 | CH3CN | 8 | 50 |
| 4 | Cu2S | 0.5 | DBU | DMF | 8 | 80 |
| 5 | Cu2S | 0.5 | DBU | CH3OH | 8 | 50 |
| 6 | Cu2S | 0.5 | DBU | DMSO | 8 | 30 |
| 7 | Cu2S | 0.5 | DBU | CH3CN | 4 | 78 |
| 8 | Cu2S | 0.1 | DBU | CH3CN | 8 | 98 |
| 9 | Cu2S | 1 | DBU | CH3CN | 8 | 90 |
| 10 | None | 0.5 | DBU | CH3CN | 8 | 0 |
| 11 | Cu2S | 0.5 | None | CH3CN | 8 | 0 |
| 12 | Commercial Cu2S | 0.5 | DBU | CH3CN | 8 | 80 |
This study further explores the universality of the cyclization of propargylamines to yield oxazolidinone compounds.57 Using several typical propargylamines with different substituents as raw materials, the reactions were carried out at room temperature (25 ± 1 °C) for 8 h, and the yields of the target products are shown in Table 2. These propargylamines efficiently generate the corresponding oxazolidinone compounds in high yields of at least 90% upon carboxylation reactions using CO2 under atmospheric pressure.
| Substrate | Product | Yieldb (%) | TON | TOF/h−1 |
|---|---|---|---|---|
| a Reaction conditions: 1 mmol substrate, 0.01 mmol catalyst, 1 atm CO2 balloon, 1 mmol DBU and 3 mL CH3CN.b Yields were determined by 1H NMR with mesitylene as the internal standard. | ||||
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99% | 99 | 12.4 |
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97% | 97 | 12.1 |
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94% | 94 | 11.8 |
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98% | 98 | 12.3 |
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97% | 97 | 12.1 |
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93% | 93 | 11.6 |
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95% | 95 | 11.9 |
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94% | 94 | 11.8 |
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93% | 93 | 11.6 |
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96% | 96 | 12.0 |
To explore the recyclability of the Cu2S catalyst, it was collected after the propargylamine transformation to oxazolidinone by reaction with CO2 and reused under the same catalytic conditions. The data are shown in Fig. 4. On the one hand, the synthesized Cu2S maintains its catalytic performance during the cyclization process and this only slightly decreases after five consecutive uses. On the other hand, the commercial Cu2S catalyst shows an obvious activity decrease after five uses. This indicates that synthesized Cu2S, unlike commercial Cu2S, shows high stability in the catalytic reaction. To further confirm that the reaction is catalyzed by the solid Cu2S surface rather than the leached copper species, a leaching test was performed (see Fig. 4c).58 The reaction mixture was filtered at approximately 48% conversion to remove the solid catalyst. The filtrate was then stirred under the same reaction conditions for an additional 4 hours. We observed that the reaction proceeded negligibly after the removal of the solid catalyst. This result strongly supports the heterogeneous nature of the catalytic system.
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| Fig. 4 Recycling performance of synthesized Cu2S (a) and commercial Cu2S (b) in the cyclization reaction of N-2-propyn-1-ylbenzenemethanamine with CO2. (c) Leaching test. | ||
To investigate the solubility of copper species under stoichiometric conditions, a mechanistic experiment was conducted using 0.3 mmol of substrates and 0.3 mmol of Cu2S (1
:
1 ratio). After the reaction, the supernatant was separated and concentrated to dryness without work-up to ensure full retention of all organic and inorganic components. ICP-MS analysis data, as shown in Table 3, revealed a total leached copper mass of 2.15 mg. Relative to the total copper input (38.13 mg), this corresponds to a leaching percentage of 5.6%. This result indicates that even when the catalyst is used in stoichiometric amounts relative to the substrate, the dissolution of active copper species remains suppressed (<6%).
| Sample | Mass of residue (mg) | Total Cu detecteda (mg) | Cu content (wt%) | Total Cu input (mg) | Leaching percentage (%) |
|---|---|---|---|---|---|
| a Reaction conditions: propargylamine (0.3 mmol), DBU (0.3 mmol), Cu2S (0.3 mmol), CH3CN.b Theoretical mass of copper in 0.3 mmol Cu2S. | |||||
| D1 | 34.95 | 1.11 | 3.17 | — | — |
| D2 | 23.41 | 0.75 | 3.18 | — | — |
| D3 | 9.18 | 0.29 | 3.12 | — | — |
| Total | 67.54 | 2.15 | 3.18 (avg.) | 38.13b | 5.64 |
Table 4 presents a comparative analysis of the catalytic efficiency of the developed system in the carboxylation reaction relative to previously reported catalytic systems. Notably, the preparation of the Cu2S catalyst does not rely on expensive or sensitive organic ligands, resulting in a simpler, lower-cost process, minimized waste generation, and reduced energy consumption, further aligning with the concept of green chemistry. This catalytic system achieves efficient conversion under mild conditions while maintaining high yields. Unlike conventional methods with poor catalyst recyclability, the Cu2S catalyst synthesized here can be easily recovered and reused at least five times, making it more suitable for large-scale or industrial applications.
| Entry | Catalyst | Base | CO2 pressure (MPa) | Solvent | Temperature (°C) | Time (h) | Yield (%) | Ref. |
|---|---|---|---|---|---|---|---|---|
| 1 | Cd-Bpy-COF | DBU | Balloon | CH3CN | 60 | 12 | 99.9 | 53 |
| 2 | Cu2O@MOF | DBU | 1.0 | CH3CN | 70 | 12 | 94 | 26 |
| 3 | Ag@2,6-FPP-TAPT | DBU | Balloon | CH3CN | 50 | 2 | 99 | 54 |
| 4 | Ag@Pybpy-COF | Cs2CO3 | 1.0 | DMF | 50 | 0.5 | 99 | 55 |
| 5 | Cu2S | DBU | Balloon | CH3CN | RT | 8 | 99 | This work |
Based on the above results and previous reports, a possible mechanism for the carboxylic cyclization of CO2 with propargylamine is proposed (Fig. 5).62–66 First, the amine reacts with CO2 with concomitant deprotonation by DBU forming the DBUH+ salt of the carbamate, which coordinates Cu through the N atom, generating intermediate A. Then, an oxygen atom of the carboxylic acid group coordinates to Cu, which shifts from N-coordination to π-alkyne coordination and activation in intermediate B. This is followed by a π to σ shift of the Cu atom, leading to isomerization to the Cu-alkenyl heterocycle C. Finally, protonation of C by DBUH+ provides the metal-free target heterocyclic product, while regenerating the Cu(I) catalyst and DBU.
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| Fig. 5 Proposed reaction mechanism for the carboxylative cyclization of N-benzylprop-2-yn-1-amine catalyzed by synthesized Cu2S. | ||
In recent years, the carboxylation of simple alkynes with CO2 catalyzed by inorganic catalysts to form propiolic acid derivatives has attracted extensive attention.67,68 For example, Yu's group69–72 has been focusing on the application of CO2 in organic synthesis. In addition to copper catalysis, these authors also used visible light photoredox catalysis to achieve efficient carboxylation cyclization to prepare propiolic acid compounds. Propiolic acid is not only a basic building block in medicinal chemistry but also a major component of bioactive compounds and conductive polymers.73
Herein, exploring the potential application of Cu2S in the green catalytic carboxylation of terminal alkynes with CO2 is also considered.74–76 To optimize the catalytic conditions, phenylacetylene is selected as a model substrate (Table 5). The heterogeneous reaction proceeded smoothly at 80 °C, yielding the target product, phenylpropiolic acid, in 82% yield within 6 hours (Table 5, entry 1). Substituting TEA or DBU for cesium carbonate reduced the yield to trace amounts (Table 5, entries 2 and 3). Changing the solvent from DMF to CH3CN or DMSO reduced the yield to trace amounts and 51%, respectively (Table 5, entries 4 and 5). Shortening the reaction time to 3 hours reduced the yield to 50% (Table 5, entry 6). After 6 hours of reaction at room temperature, trace amounts of the target product, phenylpropiolic acid, were afforded (Table 5, entry 7). Lewis acids are known to promote the carboxylation of alkynes by binding to one or both oxygen atoms of CO2, further promoting C–C bond formation with CO2 (see SI, Fig. S3). Adding the Lewis acid cocatalyst GaBr3 under the conditions of entry 1 further improved the yield to 99% (Table 5, entry 8). Changing the substrate dosage from 0.5 mmol to 0.1 mmol and 1 mmol resulted in yields of 99% and 92%, respectively (Table 5, entries 9 and 10). In the absence of catalyst or base, only trace amounts of the desired product were produced (Table 5, entries 11 and 12). Subsequently, under the same catalytic conditions as entry 8 (including the presence of GaBr3), commercially available Cu2S catalyzed the reaction, yielding only 81% of the product (Table 5, entry 13). These results indicate that the synthesized Cu2S is an efficient catalyst (more efficient than commercial Cu2S) and achieves the green conversion of phenylacetylene with CO2. The efficiency of the reaction, which is already very good in the absence of Lewis acid co-catalyst, is even increased under the action of the co-catalyst GaBr3.
| Entry | Catalyst | Substrate (mmol) | Base | Solvent | t (h) | T (°C) | Yieldb (%) |
|---|---|---|---|---|---|---|---|
| a Reaction conditions: phenylacetylene (0.5 mmol), Cu2S (0.005 mmol), GaBr3 (0.005 mmol), Cs2CO3 (0.75 mmol), DMF (3 mL), CO2 (balloon).b Isolated yield. | |||||||
| 1 | Cu2S | 0.5 | Cs2CO3 | DMF | 6 | 80 | 82 |
| 2 | Cu2S | 0.5 | TEA | DMF | 6 | 80 | Trace |
| 3 | Cu2S | 0.5 | DBU | DMF | 6 | 80 | Trace |
| 4 | Cu2S | 0.5 | Cs2CO3 | CH3CN | 6 | 80 | Trace |
| 5 | Cu2S | 0.5 | Cs2CO3 | DMSO | 6 | 80 | 51 |
| 6 | Cu2S | 0.5 | Cs2CO3 | DMF | 3 | 80 | 50 |
| 7 | Cu2S | 0.5 | Cs2CO3 | DMF | 6 | 25 | Trace |
| 8 | Cu2S/GaBr3 | 0.5 | Cs2CO3 | DMF | 6 | 80 | 99 |
| 9 | Cu2S/GaBr3 | 0.1 | Cs2CO3 | DMF | 6 | 80 | 99 |
| 10 | Cu2S/GaBr3 | 1 | Cs2CO3 | DMF | 6 | 80 | 92 |
| 11 | None | 0.5 | Cs2CO3 | DMF | 6 | 80 | Trace |
| 12 | Cu2S/GaBr3 | 0.5 | None | DMF | 6 | 80 | Trace |
| 13 | Commercial Cu2S/GaBr3 | 0.5 | Cs2CO3 | DMF | 6 | 80 | 81 |
The carboxylation of terminal alkynes toward the synthesis of propiolic acid derivatives was further explored. Several typical terminal alkynes with different substituents were used as raw materials and reacted at 80 °C for 6 h. The yields of the target products are shown in Table 6. Most yields are higher than 90%. This result indicates that most terminal alkynes efficiently generate the corresponding propiolic acid derivatives and in high yield under these conditions.
Based on the above results and some previous reports,69,72,75,76 a possible mechanism of action of the Cu2S catalyst is proposed (Fig. S3). First, the terminal alkyne coordinates with Cu(I), and Cs2CO3 deprotonates the terminal alkyne to generate Cu(I) acetylide intermediate B. At the same time, CO2 inserts into the carbon–copper bond, while Ga(III) coordinates with the oxygen atom to generate copper propiolate intermediate C. The copper propiolate intermediate C then reacts with free Cs ions to release cesium propiolate. At the end of the reaction, cesium propiolate is acidified to obtain the propiolic product.
1H NMR and 13C spectra were recorded at 25 °C using a Bruker AC 300 MHz instrument. All chemical shifts are reported in parts per million (δ, ppm) and calibrated using residual protons in deuterated solvents (CDCl3 at 7.26 ppm for 1H NMR and 77.16 ppm for 13C NMR; CD3OD at 3.31 ppm for 1H NMR and 49.00 ppm for 13C NMR). The contents of carbon, hydrogen, oxygen, nitrogen, and sulfur were determined using a FlashSmart™ Elemental Analyzer (Thermo Scientific™).
The powder X-ray diffraction data were collected at room temperature on a PANalytical X'Pert MPD diffractometer (45 kV, 40 mA) equipped with a fast PIXcel 1D detector with Cu Kα1,2 radiation in the range 6° < 2θ < 60° 2θ, a step size of 0.013° 2θ and a counting time of 38 s per step. Powdered samples were spread on a glass sampling holder. The data have been compared with the PDF5+ database from ICDD.
The supernatant after the catalytic reaction is dried under vacuum to remove the solvent. The sample was divided into three aliquots of varying masses. Each portion was weighed into a clean, sterile 15 mL polypropylene centrifuge tube (Fisherbrand™ Easy Reader™). Reagents were added sequentially to each tube under a fume hood: 375 µL of H2O2, 525 µL of HNO3, and 100 µL of HCl (total volume: 1.0 mL). Upon addition of HNO3, the solution became clear, and a tawny (HEX #C68346) precipitate was observed, indicating the presence of copper. This precipitate disappeared upon the addition of HCl. The digestion process lasted over 96 hours. At this point, all samples were completely digested, and the solutions were clear with no visible precipitate. The final digests were analyzed using a iCAP-Q ICP-MS equipment (Thermo Scientific, Bremen, Germany) equipped with an autosampler ASX-500 (CETAC Technologies, Omaha, USA).
XPS spectra were recorded using the PHI XPS VersaProbe III energy spectrometer equipped with a monochromatic 1486.6 eV Al-Kα radiation source. A focused X-ray source with X-ray beam size of 100 μm, power of 25 W, and e-beam energy of 15 kV was used. Charge neutralization was possible by using a complementary dual-beam charge neutralization method. The C 1s peak at 284.8 eV was used as the reference signal to calibrate all acquired spectra. A pass energy of 13 eV was used for the acquisition of all high-resolution spectra.
For the High-Resolution Transmission Electron Microscopy (HR-TEM) studies, samples were dispersed in hexane. Before drop casting on ultrathin carbon film placed on lacey carbon Au-coated grids (Ted Pella Inc., USA), dispersions were subjected to soft sonication until they became homogeneous. The grids were left to dry under ambient conditions prior to investigation. HR-TEM experiments were conducted on a JEOL JEM-2100F UHR electron microscope (200 kV) equipped with an Energy Dispersive X-ray (EDS) detector (Oxford UltimMax) and two Scanning Transmission Electron Microscopy (STEM) detectors: Bright-Field (BF) and High-Angle Annular Dark-Field (HAADF). Flash column chromatography was performed using silica gel (300–400 mesh).
:
1 as an eluent) to afford the pure product. Finally, the pure products were characterized by 1H NMR and 13C NMR. In the recycling experiments, the catalyst is separated by centrifugation and washed three times with CH3CN. Thereafter, the catalyst is dried at 60 °C overnight before its next use.
Supplementary information (SI): general procedure for the synthesis of propargylic amines; Table S1: Analysis summary of the high-resolution Cu 2p XPS; Fig. S1: High-resolution valence band XPS and Cu Auger signals; Table S2: Analysis summary of the Cu Auger parameter; Fig. S2: High-resolution S 2p XPS; Table S3: Analysis summary of the high-resolution S 2p XPS; Fig. S3: Proposed mechanism for the carboxylative cyclization of terminal alkyne catalyzed by Cu2S; 1H NMR and 13C NMR data and spectra for the substrates and the targeted products. See DOI: https://doi.org/10.1039/d5qi02546j.
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