Arash Ghorbani-Choghamarani*a,
Ali Ashraf Derakhshana,
Maryam Hajjamia and
Laleh Rajabib
aChemistry Department, Faculty of Science, Ilam University, Ilam, Iran. E-mail: a.ghorbani@mail.ilam.ac.ir; arashghch58@yahoo.com
bPolymer Research Lab, Department of Chemical Engineering, Razi University, Kermanshah, Iran. E-mail: laleh.rajabii@gmail.com
First published on 28th September 2016
Herein for the first time, a mesoporous copper nano catalyst (SBA–Cu2+) were simply synthesized through immobilization of Cu2+ on surface of Schiff base alumoxane support. This nano catalyst was characterized by various techniques such as FT-IR, X-ray map, TG-DTA, BET, SEM, SEM-EDS, TEM, ICP-OES and XRD. The characterization results indicated that SBA–Cu2+ nanoflakes with 331.47 m2 g−1 specific surface area are thermally stable up to 306 °C. The SBA–Cu2+ nano catalysts showed significant activity for Suzuki–Miyaura and Stille cross-coupling reactions with good efficiency and reusability. In addition, the nanocatalyst could be recovered and reused several times without significant loss of its catalytic activity. Copper leaching from SBA–Cu2+ is very negligible for this coupling reaction.
Despite the widespread applications as a catalyst, homogeneous Pd complexes have limiting aspects such as toxicity and high price which led to limitations on industrial scale applications.4 As a viable alternative for Pd, recently copper-based catalysts have attracted much attention due to their biocompatibility and lower price as well as their catalytic aptitude for cross-coupling reactions.5 Despite these advantages, only a few Suzuki or Stille reactions involving copper catalyzed cross-coupling have been reported. These copper based catalysts are including Cu/Schiff-base@Fe3O4,6 Cu nano colloid,7 3D MOF {[Cu(4-tba)2](solvent)}n,8 Cu@molecular sieve9 and Pd–Cu@carbon.10 Thus, to expand the copper catalyzed Suzuki or Stille coupling reactions, the development of new and efficient nano catalysts based on Cu is necessary. In this way, the use of novel materials as a catalyst support is inevitable. Immobilization of Cu species on solid supports in heterogeneous catalysts facilitates separation, minimizing contamination and reusability of expensive catalysts. In order to preparation of heterogeneous catalysts, various solid supports including polymers, zeolites, silica, carbon nanotubes and metal–organic frameworks (MOFs) have been utilized.11 The nature of supports can influence the selectivity and reactivity of the catalyst, therefore careful choice of supports can be led to creation of new heterogeneous catalysts. As a new suggestion, the carboxylate–alumoxane is a versatile compound which can be introduce as a novel support for heterogeneous catalysts. Carboxylate alumoxanes with general formula [Al(O)x(OH)y(O2CR)z]n, 2x + y + z = 3 are prepared from the reaction of boehmite (γ-AlOOH) and carboxylic acids. The surface of the alumoxanes is covered with covalently bound carboxylate groups. The physical and chemical properties of the alumoxane can be affected by the type of carboxylic acid, and range from water soluble powders to hard solids that are resistant to acids, bases and organic solvents.12,13 As a precursor for alumoxane synthesis, boehmite is a metastable phase of aluminium oxide with oxide–hydroxide bonds which commonly used as supporting matrix.14,15 The advantages of alumoxane as a catalyst support are included the low price of boehmite and the availability of an almost infinite range of carboxylic acids.16 The only report on the catalytic used of alumoxane were related to zirconocene complex supported on para-hydroxybenzoate-alumoxane (PHBA) as novel catalyst for olefin polymerization.17 Nevertheless, there is no significant works about application of alumoxanes in the catalysis field especially for C–C coupling reactions.
Currently there is no report about using the alumoxane supports for Suzuki–Miyaura and Stille reactions.
In order to prepare new alumoxane catalysts, Schiff bases ligands can play an important role in complexing of metal cations on alumoxane surface. Therefore the using of carboxylic Schiff-base molecules in the synthesis of alumoxane can be led to formation of novel catalyst support. In this work for the first time we report the successful synthesis of copper–alumoxane nano catalyst through immobilization of Cu2+ on Schiff-base alumoxane and using them as a new nanocatalyst for the Suzuki–Miyaura and Stille coupling reaction (Fig. 1).
In the spectrum of SBA (Fig. 2b), there are several peaks in 1200–1800 cm−1 region which are indicated formation of carboxylate–alumoxane through the covalent bonding between Bo and SB. The two absorption peaks in 1560 and 1492 cm−1 are related to the asymmetrical and symmetrical stretching vibrations of bidentate carboxylate groups, respectively. As well as the frequency of 1626 cm−1 is due to unidentate carboxylate bonds.12,18 The Schiff base shows the CN vibrations in the frequency of 1663 cm−1 while phenolic C–O stretching vibrations are observed at 1282 cm−1. Also the two frequencies at 1600 and 1417 cm−1 are due to the vibrations of sp2 C
C in the benzene rings.19 In the spectrum of SBA–Cu2+ (Fig. 2c), decreasing in intensity of C
N peak (1663 cm−1) is referred to chelation of Cu2+ by SBA ligands. It seems that chelation caused to reduce in bond vibrations. Also to increase in peak of 1560 cm−1 can be due to vibration of acetate ligand which connected to the Cu2+.19 It seems that some of the Al–OH groups in boehmite nanoparticles cannot be reacted with Schiff base SB. Because the boehmite index peaks in SBA and SBA–Cu2+ spectra have been existence. According to the literature,19 the stretching frequencies of Cu–O and Cu–N emerge at 431–455 and 555–470 cm−1 for Cu–Schiff base complex. But in the SBA–Cu2+, these stretching peaks have covered with overlapping of Al–O–Al stretching modes in the range of 400–800 cm−1.
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Fig. 3 N2 adsorption–desorption isotherms and the corresponding pore size distributions for boehmite nanoparticles (a and b) and SBA–Cu2+ (c and d). |
Table 1 is presented all data attained by Brunauer–Emmett–Teller (BET) and Barrett–Joyner–Halenda (BJH) methods. The specific surface area (SBET) for Bo precursor is 2.28 m2 g−1, with 22 nm average pore diameter and a specific pore volume of 0.0125 cm3 g−1. Despite of our expectation, boehmite nano particles (Bo) have shown the very low surface area, which can be due to sever agglomeration among them. In return, SBA–Cu2+ with the specific surface area (SBET) of 331.47 m2 g−1 and average pore diameter 9.91 nm has shown a specific pore volume of 0.8217 cm3 g−1. It seems that alumoxane formation is caused to reduce in extent of agglomeration and increasing of surface area. The Dav for boehmite (Bo) and SBA–Cu2+ illustrated meso porosity while DBJH values showed the micro porosity for them.
Sample | Specific surface area [m2 g−1] | Specific pore volume [cm3 g−1] | Pore diameter [nm] | |||
---|---|---|---|---|---|---|
SBET | SBJH | Vtot (BET) | V (BJH) | Dav | D (BJH) | |
Boehmite | 2.28 | 2.48 | 0.0125 | 0.0125 | 22 | 1.21 |
SBA–Cu2+ | 331.47 | 397.13 | 0.8217 | 0.8404 | 9.91 | 1.64 |
The wide angle XRD pattern of Bo (Fig. 4b) indicates broad peaks at 2θ = 14°, 28.1°, 38.5°, 45.7°, 49.2°, 51.2°, 55.2°, 61°, 64.3°, 67°, 68.3°, 72° and 81° which can be attributed to the orthorhombic unit cell of boehmite γ-AlOOH (JCPDS card 21-1307). The low intensity and broadening peaks shows that Bo nanoparticles had low crystallinity.
Just like Bo, the XRD pattern of SBA (Fig. 4b) revealed the same diffraction lines but sharper and more intense than Bo. This may be due to inadequate functionalization of Bo with Schiff-base molecules because of some spherical hindrances. Also increasing in sharpness and intensity of peaks represents its higher crystallinity. In the other hand, the XRD spectrum of SBA–Cu2+ (Fig. 4b) illustrated the same sharp diffraction peaks of SBA. The emersion of new peaks at 2θ = 33.5°, 35.5°, 37.2°, 57.2°, 62.5°, 77.3° and 91.1° are related to the Cu2+ and CuO in the catalyst.20
Fig. 5b exhibited that the morphology of SBA is significantly different from Bo. The SBA sample has the morphology of irregular nano flakes with about 20–30 nm thickness and 50–100 nm across. It can be seen from Fig. 5c the chelation of Cu2+ by SBA was led to roughen the surface of nano flakes. The magnified images and their schematics illustrate significantly the morphology of SBA–Cu2+ catalyst (Fig. 5d). The TEM images confirmed the morphology of SBA–Cu2+ and well distribution of Cu2+ at the surface of mesoporous nano flakes (Fig. 6). It can be seen that SBA–Cu2+ has to some extent cubic or hexagonal structures.
The expected elements in the structure of Bo, SBA and SBA–Cu2+ can be detected by SEM-EDS analysis presented in the Fig. 7. For Bo sample the percentage of C, O and Al in Fig. 7a have been recorded. In comparing with Bo, The SBA sample shows 3.8% w for N element which confirms the presence of Schiff-base molecules (Fig. 7b). The EDS data for SBA–Cu2+ also confirms the presence of Cu2+ on the surface of SBA supports with the weight present about 7.79% w (Fig. 7c).
The X-ray mapping of SBA–Cu2+ were recorded in order to evaluate the dispersion of Cu active sites in the catalyst. Fig. 8 shows the elemental map images which confirmed the good dispersion of Cu on surface of catalyst. Also the dispersion of N in the surface are indicated the presence of Schiff-base ligands in the catalyst.
The second step weight loss (mass change: 10.1%) is mainly initiated at 267 °C which DTA curve shows an exothermic peak at 306 °C. This step is referred to thermal decomposition of complex. The third step weight loss (mass change: 12.69%) may be related to the phase transfer of boehmite structure to the alumina phase which can be accompanied by OH elimination. Because in SBA–Cu2+ there are some free Al–OH groups that could not reacted with Schiff-base molecules. For this process, the DTA curve shows an endothermic peak at 475 °C.
In our primary experiments, Suzuki–Miyaura reaction between iodobenzene and sodium tetraphenylborate (NaBPh4) was selected as a model reaction to optimize the effects of base, solvent, temperature and amount of SBA–Cu2+.
Unlike common boronic acid or esters, the prominent advantage of NaBPh4 is that it can react with four equivalents of electrophilic reagents. Therefore in aspect of economic and environmental concerns, this is a green protocol in organic synthesis. Despite this benefits, only a few works involving NaBPh4 for coupling reaction have been reported. Thus, to expand the scope and reactivity of sodium tetraphenyl borate, the development of new and efficient catalytic protocols is necessary.23
Table 2 presents the results of optimization conditions. Firstly, 4 to 11 mg of catalyst was used to catalyze the model reaction at 80 °C in the presence of Na2CO3 and PEG as solvent. The best result was obtained using 10 mg (0.379 × 10−5 mol g−1) of catalyst (Table 2, entry 8). While, there was no significant improvement in the reaction yield by increasing the amount of catalyst (Table 2, entry 9).
Entry | Solvent | Base | Catalyst [mg] | Temp [°C] | Time [min] | Yieldb [%] |
---|---|---|---|---|---|---|
a Reaction conditions: iodobenzene (1 mmol), NaPh4B (0.5 mmol), PEG (2 mL), and 3 mmol base.b Isolated yield. | ||||||
1 | PEG | Na2CO3 | — | 80 | 180 | — |
2 | PEG | Na2CO3 | 4 | 80 | 120 | Trace |
3 | PEG | Na2CO3 | 5 | 80 | 60 | 15 |
4 | PEG | Na2CO3 | 6 | 80 | 60 | 38 |
5 | PEG | Na2CO3 | 7 | 80 | 60 | 58 |
6 | PEG | Na2CO3 | 8 | 80 | 30 | 70 |
7 | PEG | Na2CO3 | 9 | 80 | 30 | 85 |
8 | PEG | Na2CO3 | 10 | 80 | 30 | 94 |
9 | PEG | Na2CO3 | 11 | 80 | 30 | 95 |
10 | PEG | NaHCO3 | 10 | 80 | 30 | 81 |
11 | PEG | NaOAc | 10 | 80 | 30 | 35 |
12 | PEG | KH2PO4 | 10 | 80 | 30 | 25 |
13 | PEG | NaOH | 10 | 80 | 30 | — |
14 | PEG | K2CO3 | 10 | 80 | 30 | — |
15 | H2O | Na2CO3 | 10 | 80 | 30 | 78 |
16 | Et-OH | Na2CO3 | 10 | 80 | 30 | 88 |
17 | DMF | Na2CO3 | 10 | 80 | 30 | 15 |
18 | DMSO | Na2CO3 | 10 | 80 | 30 | Trace |
19 | PEG | Na2CO3 | 10 | 25 | 180 | — |
20 | PEG | Na2CO3 | 10 | 45 | 180 | 17 |
21 | PEG | Na2CO3 | 10 | 60 | 30 | 45 |
22 | PEG | Na2CO3 | 10 | 100 | 20 | 96 |
In order to find out the best base for this coupling reaction, the model reaction was evaluated in presence of NaHCO3, NaOAc, KH2PO4, NaOH and K2CO3 (Table 2, entries 10–14). So the results were confirmed that Na2CO3 is the best base among them. No product has been obtained in using of NaOH or K2CO3 as a base. It seems that the strength of these base caused to the by-reactions. NaOH and K2CO3 are the strongest base among other bases based on their Kb values. Knecht and co-workers21 have reported that the amount of free and reactive OH– for KOH or NaOH is higher than Na2CO3 and NaHCO3 bases, which caused to a strong combination with metal species leading to a decrease in biphenyl yield. Therefore, it seems that high level of free hydroxide in entries 13 and 14 have strong combination with Cu species or strong reaction with NaBPh4 which caused to destroy the Suzuki reaction.
The effects of various solvents on the model reaction were studied by using Et-OH, DMSO, H2O and DMF instead of PEG (Table 2, entries 15–18). The results show that the PEG was more effective than other solvents. Despite aprotic solvents (DMSO and DMF), it seems that the protic solvents (PEG, Et-OH and H2O) have better effect on the coupling reaction catalyzed by SBA–Cu2+. It may be referred to the positive interactions between protic solvent and polar functional groups in SBA–Cu2+ which can be help to effective dispersion. In the other side, the PEG as a phase transfer catalyst can enhance the solubility of the reagents (aryl halide, NaBPh4, base), as well as promote basicity of Na2CO3. The alcoholic solvent as a protic solvent have shown better yield than water because of its better polarity to dissolve reagents.
In continuous, it found that the reaction yields were impressionable to temperature factor. So, the effect of various temperature were studied in rang of 25 to 100 °C (Table 2, entries 19–22) and the best results were obtained at 80 °C (Table 2, entry 8). After optimizing the conditions, a series of aryl halides, which contain different substitution groups, such as electron-donating and electron-withdrawing were used for the synthesis of biphenyl derivatives in the presence of SBA–Cu2+. Table 3 shows the summarized results of this study in the optimized conditions (10 mg catalyst, Na2CO3 as base in PEG solvent at 80 °C).
Entry | R | X | Time (min) | Yieldb [%] | Mp (°C) | TON | TOF (h−1) | |
---|---|---|---|---|---|---|---|---|
Found | Reported | |||||||
a Reaction conditions: aryl halides (1 mmol), NaPh4B (0.5 mmol), PEG (2 mL), Na2CO3 (3 mmol), SBA–Cu2+ catalyst (10 mg, 0.379 mol%) and 80 °C.b Isolated yield.c Containing 20 mg nano catalyst and 95 °C reaction temperature. | ||||||||
1 | H | I | 30 | 94 | 68–69 | 68–70 (ref. 22) | 248 | 496 |
2 | 4-CH3 | I | 80 | 91 | 45–47 | 44–46 (ref. 22) | 240 | 180 |
3 | 2-COOH | I | 90 | 89 | 108–110 | 111–113 (ref. 2) | 235 | 156 |
4 | 4-MeO | I | 95 | 92 | 85–87 | 88–90 (ref. 22) | 242 | 153 |
5 | H | Br | 40 | 90 | 68–69 | 68–70 (ref. 22) | 237 | 355 |
6 | 4-NO2 | Br | 160 | 92 | 111–113 | 112–114 (ref. 22) | 242 | 91 |
7 | 4-CN | Br | 180 | 91 | 83–84 | 85–86 (ref. 23) | 240 | 80 |
8 | 4-Cl | Br | 120 | 89 | 74–75 | 77–79 (ref. 22) | 235 | 117 |
9 | 4-CH3 | Br | 110 | 91 | 45–47 | 44–46 (ref. 22) | 240 | 131 |
10 | 4-OH | Br | 170 | 88 | 161–163 | 163–164 (ref. 23) | 232 | 82 |
11 | 1-Br-naphthalene | Br | 600 | 55 | Colorless oil | Colorless oil (ref. 24) | 145 | 14 |
12 | H | Cl | 360 | 64 | 66–69 | 68–70 (ref. 22) | 168 | 28 |
13 | 4-CN | Cl | 480 | 28c | 83–84 | 85–86 (ref. 23) | 37 | 4.6 |
14 | 4-Iodopyridine | 40 | 86 | 66–68 | 69–70 (ref. 25) | 227 | 325 | |
15 | 4-Bromopyridine | 45 | 80 | 66–68 | 69–70 (ref. 25) | 201 | 268 |
As expected, the Suzuki reaction for aryl iodides gave the best yields in the shorter times (Table 3, entries 1–4). Aryl bromides have shown high reactivity but relatively in longer reaction times versus aryl iodides (Table 3, entries 5–11). And regularly, the coupling of aryl chlorides were done in more difficult conditions that led to the lower yields (Table 3, entries 12–13).
Overall, electronic effects have an effect on Suzuki reaction, so that aryl halides with electron-donating groups gave little higher yields than those with electron-withdrawing groups. ortho-Substituted aryl halides with (Table 3, entry 3) gave lower yields than those at para-substituted, which reveals that steric hindrance has a negative effect on the Suzuki reaction.
Using the hetero aryl halides (Table 3, entries 14 and 15) shows the lower yields in compare with ordinary aryl halides these can be due to withdrawing effect of heteroatom in aryl halide.
In order to demonstrate applications of the SBA–Cu2+ as an active catalyst, it was evaluated in the C–C coupling through Stille reaction. Therefore, the reaction of iodobenzene and triphenyltin chloride were selected as a model reaction to obtain optimized conditions. In this way Table 4 shows the results of various conditions in model reaction. No product has been achieved without SBA–Cu2+ catalyst (Table 4, entry 1). Similar to the Suzuki–Miyaura reaction, the best amount of nano catalyst were chosen 10 mg (0.379 × 10−5 mol g−1) of the SBA–Cu2+ (Table 4, entry 8). No significant improvement in yield was detected through increasing the amount of the SBA–Cu2+ (Table 4, entry 9). Using the various base in the model reaction indicated that sodium carbonate was still the more efficient base among them (Table 4, entries 10–13).
Entry | Solvent | Base | Catalyst [mg] | Temp [°C] | Time [min] | Yieldb [%] |
---|---|---|---|---|---|---|
a Reaction conditions: iodobenzene (1 mmol), triphenyltin chloride (0.5 mmol), PEG (2 mL), and 3 mmol base.b Isolated yield. | ||||||
1 | PEG | Na2CO3 | — | 80 | 240 | — |
2 | PEG | Na2CO3 | 4 | 80 | 60 | Trace |
3 | PEG | Na2CO3 | 5 | 80 | 50 | 14 |
4 | PEG | Na2CO3 | 6 | 80 | 50 | 32 |
5 | PEG | Na2CO3 | 7 | 80 | 50 | 54 |
6 | PEG | Na2CO3 | 8 | 80 | 20 | 70 |
7 | PEG | Na2CO3 | 9 | 80 | 20 | 81 |
8 | PEG | Na2CO3 | 10 | 80 | 20 | 93 |
9 | PEG | Na2CO3 | 11 | 80 | 20 | 94 |
10 | PEG | NaHCO3 | 10 | 80 | 20 | 71 |
11 | PEG | NaOAc | 10 | 80 | 20 | 55 |
12 | PEG | KH2PO4 | 10 | 80 | 20 | 43 |
13 | PEG | K2CO3 | 10 | 80 | 20 | 18 |
14 | H2O | Na2CO3 | 10 | 80 | 20 | 76 |
15 | Et-OH | Na2CO3 | 10 | 80 | 20 | 89 |
16 | DMF | Na2CO3 | 10 | 80 | 20 | 32 |
17 | DMSO | Na2CO3 | 10 | 80 | 20 | 22 |
18 | PEG | Na2CO3 | 10 | 25 | 240 | Trace |
19 | PEG | Na2CO3 | 10 | 45 | 120 | 52 |
20 | PEG | Na2CO3 | 10 | 60 | 70 | 74 |
21 | PEG | Na2CO3 | 10 | 100 | 15 | 95 |
In continuous, evaluation of various solvents in model reaction confirmed that the PEG is the best and effective solvent among them (Table 4, entries 14–17). As previously mentioned, PEG as a protic solvent have acted as phase transfer catalyst. Also ethanol as a protic solvent have shown better yield than water because of its better polarity to dissolve reagents. Finally, the temperatures in ranging from 25 to 100 °C were chosen to evaluate of the temperature effect in model reaction (Table 4, entries 8 and 18–21). It was found that the reaction catalyzed effectively at 80 °C (Table 4, entry 8). As mentioned above, the best results are obtained with 10 mg (0.379 mol%) of SBA–Cu2+ in PEG solvent at 80 °C and using Na2CO3 (Table 4, entry 8). After optimization the reaction, various aryl halides with triphenyltin chloride were employed in Stille reaction for the synthesis of biphenyl derivatives. Table 5 summarized the results of this study. These results reveal that various aryl halides with electron-donating and electron-withdrawing substituents were catalyzed equally facile by SBA–Cu2+ in appropriate yields and lower times. As expected aryl iodides and bromides reacted in shorter times in compared to aryl chlorides.
Entry | R | X | Time (min) | Yieldb [%] | Mp (°C) | TON | TOF (h−1) | |
---|---|---|---|---|---|---|---|---|
Found | Reported | |||||||
a Reaction conditions: aryl halides (1 mmol), triphenyltin chloride (0.5 mmol), PEG (2 mL), Na2CO3 (3 mmol), SBA–Cu2+ catalyst (10 mg, 0.379 mol%) and 80 °C.b Isolated yield. | ||||||||
1 | H | I | 20 | 93 | 68–69 | 68–70 (ref. 22) | 245 | 735 |
2 | 4-CH3 | I | 120 | 90 | 45–47 | 44–46 (ref. 22) | 237 | 118 |
3 | 2-COOH | I | 125 | 89 | 108–110 | 111–113 (ref. 2) | 235 | 113 |
4 | 4-MeO | I | 100 | 86 | 85–87 | 88–90 (ref. 22) | 227 | 136 |
5 | H | Br | 25 | 92 | 68–69 | 68–70 (ref. 22) | 243 | 583 |
6 | 4-NO2 | Br | 75 | 90 | 111–113 | 112–114 (ref. 22) | 237 | 190 |
7 | 4-CN | Br | 80 | 91 | 83–84 | 85–86 (ref. 23) | 240 | 180 |
8 | 4-Cl | Br | 120 | 85 | 74–75 | 77–79 (ref. 22) | 224 | 112 |
9 | 4-CH3 | Br | 100 | 89 | 45–47 | 44–46 (ref. 22) | 235 | 141 |
10 | 4-OH | Br | 120 | 87 | 161–163 | 163–164 (ref. 23) | 229 | 114 |
11 | 1-Br-naphthalene | Br | 420 | 59 | Colorless oil | Colorless oil (ref. 24) | 155 | 22 |
12 | H | Cl | 240 | 67 | 66–69 | 68–70 (ref. 22) | 177 | 44 |
13 | 4-Iodopyridine | 30 | 88 | 66–68 | 69–70 (ref. 25) | 222 | 443 | |
14 | 4-Bromopyridine | 40 | 82 | 66–68 | 69–70 (ref. 25) | 206 | 310 |
Also in Stille reaction, using the hetero aryl halides (Table 5, entries 13 and 14) indicates the moderate yields in compare with ordinary aryl halides these can be due to withdrawing effect of heteroatom in aryl halide.
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Fig. 10 Recycling and reusability of SBA–Cu2+ in the coupling reaction of iodobenzene (1 mmol) with (a) NaBPh4 (0.5 mmol) and (b) Ph3SnCl (0.5 mmol). |
Entry | Substrate | Reagent | Catalyst type | Cu mol% | Time (min) | Temp (°C) | Yield (%) | Ref. |
---|---|---|---|---|---|---|---|---|
1 | Ph-I | Ph-B(OH)2 | Fe3O4@SiO2–isatin–Cu2+ | 0.82 | 300 | 70 | 92 | 6 |
2 | Ph-I | Ph-B(OH)2 | Cu nano colloid | 2 | 360 | 110 | 62 | 7 |
3 | Ph-I | Ph-B(OH)2 | 3D MOF {[Cu(4-tba)2](solvent)}n | — | — | 25 | 88 | 8 |
4 | Ph-I | Ph-B(OH)2 | Cu–Pd@4A molecular sieve | 9 | 60 | 78 | 99 | 9 |
5 | Ph-I | Ph-B(OH)2 | Cu@4A molecular sieve | 9 | 60 | 78 | 62 | 9 |
6 | Ph-I | Ph-B(OH)2 | Pd–Cu/carbon | 0.99 | 180 | 78 | 97.5 | 10 |
7 | Ph-Br | Ph4BNa | Pd2+@polystyrene | 1 | 18 | 120 | 90 | 11 |
8 | Ph-I | Ph4BNa | SBA–Cu2+ | 0.379 | 30 | 80 | 94 | This work |
9 | Ph-Br | Ph4BNa | SBA–Cu2+ | 0.379 | 40 | 80 | 90 | This work |
Prior to the analysis, degassing was done for all samples at 373 K in a vacuum line for 5 h. 1H NMR spectra were recorded on a Bruker AVANCE DPX-400 (400 MHz for 1H). Chemical shifts are given in ppm (δ) relative to internal TMS and coupling constants Jare reported in Hz. The Cu content of the catalyst was measured with an inductively coupled plasma atomic emission spectrometer (ICP-OES simultaneous, Varian VISTA-PRO Model). The ultrasonic bath (240 W-35 kHz, SONREX, DT52 H, Bandelin, Germany) has been utilized for ultra-sonication of solutions.
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