| Literature DB >> 35433633 |
Mohammad Hosein Sayahi1, Mansoureh Toosibashi2, Mehdi Bahmaei1, Hosein Lijan2, Leila Ma'Mani3, Mohammad Mahdavi4, Saeed Bahadorikhalili5.
Abstract
In this study, a novel catalyst is introduced based on the immobilization of palladium onto dipyrido (3,2-a:2',3'-c) phenazine-modified mesoporous silica nanoparticles. The dipyrido (3,2-a:2',3'-c) phenazine (Py2PZ) ligand is synthesized in a simple method from the reaction of 1,10-phenanthroline-5,6-dione and 3,4-diaminobenzoic acid as starting materials. The ligand is used to functionalize mesoporous silica nanoparticles (MSNs) and modify their surface chemistry for the immobilization of palladium. The palladium-immobilized dipyrido (3,2-a:2',3'-c) phenazine-modified mesoporous silica nanoparticles (Pd@Py2PZ@MSNs) are synthesized and characterized by several characterization techniques, including TEM, SEM, FT-IR, TGA, ICP, XRD, and EDS analyses. After the careful characterization of Pd@Py2PZ@MSNs, the activity and efficiency of this catalyst is examined in carbon-carbon bond formation reactions. The results are advantageous in water and the products are obtained in high isolated yields. In addition, the catalyst showed very good reusability and did not show significant loss in activity after 10 sequential runs.Entities:
Keywords: Heck reaction; Suziki reaction; immobilized catalyst; mesoporous silica nanoparticles; palladium catalyst
Year: 2022 PMID: 35433633 PMCID: PMC9008749 DOI: 10.3389/fchem.2022.838294
Source DB: PubMed Journal: Front Chem ISSN: 2296-2646 Impact factor: 5.221
SCHEME 1Synthesis of the Pd@Py2PZ@MSN catalyst.
FIGURE 1(A) TEM; (B) SEM; (C) EDS; and (D) XRD results of the Pd@Py2PZ@MSN catalyst.
FIGURE 2(A) FT-IR; and (B) TGA results of the Pd@Py2PZ@MSN catalyst.
Surface area and pore size results of MSN and the Pd@Py2PZ@MSN catalyst.
| Surface area (m2.g−1) | Pore width (nm) | Pore volume (cm3.g−1) | |
|---|---|---|---|
| MSN | 655.65 | 5.75 | 0.79 |
| Pd@Py2PZ@MSN | 612.37 | 5.14 | 0.72 |
Optimization of the reaction of styrene and phenyl bromide in the presence of the Pd@Py2PZ@MSN catalyst.
| Entry | Solvent | Base (mol) | Catalyst (mol%) | Time (min) | Yield (%) |
|---|---|---|---|---|---|
| 1 | EtOH | TEA (1.5) | Pd@Py2PZ@MSN (1.0) | 120 | 61 |
| 2 | MeOH | TEA (1.5) | Pd@Py2PZ@MSN (1.0) | 120 | 67 |
| 3 | CH2Cl2 | TEA (1.5) | Pd@Py2PZ@MSN (1.0) | 120 | 47 |
| 4 | DMF | TEA (1.5) | Pd@Py2PZ@MSN (1.0) | 120 | 59 |
| 5 | H2O | TEA (1.5) | Pd@Py2PZ@MSN (1.0) | 120 | 94 |
| 6 | H2O | NaOH (1.5) | Pd@Py2PZ@MSN (1.0) | 120 | 80 |
| 7 | H2O | KOH (1.5) | Pd@Py2PZ@MSN (1.0) | 120 | 87 |
| 8 | H2O | Pyridine (1.5) | Pd@Py2PZ@MSN (1.0) | 120 | 69 |
| 9 | H2O | K2CO3 | Pd@Py2PZ@MSN (1.0) | 120 | 77 |
| 10 | H2O | No base | Pd@Py2PZ@MSN (1.0) | 120 | Trace |
| 11 | H2O | TEA (0.5) | Pd@Py2PZ@MSN (1.0) | 120 | 55 |
| 12 | H2O | TEA (1.0) | Pd@Py2PZ@MSN (1.0) | 120 | 70 |
| 13 | H2O | TEA (2.0) | Pd@Py2PZ@MSN (1.0) | 120 | 94 |
| 14 | H2O | TEA (1.5) | Pd@Py2PZ@MSN (0.5) | 120 | 46 |
| 15 | H2O | TEA (1.5) | Pd@Py2PZ@MSN (1.5) | 120 | 94 |
| 16 | H2O | TEA (1.5) | Pd@Py2PZ@MSN (1.0) | 60 | 67 |
| 17 | H2O | TEA (1.5) | Pd@Py2PZ@MSN (1.0) | 150 | 94 |
| 18 | H2O | TEA (1.5) | Pd/C (1.0) | 120 | 56 |
| 19 | H2O | TEA (1.5) | Pd(OAc)2 (1.0) | ″ | 69 |
| 21 | H2O | TEA (1.5) | PdCl2 (1.0) | ″ | 61 |
| 22 | H2O | TEA (1.5) | No catalyst | ″ | 0 |
Reaction conditions: styrene (1 mmol); phenyl bromide (1 mmol); catalyst; solvent (5 ml); base; 25°C.
Scope and generality of the Pd@Py2PZ@MSN catalyst in Heck and Suzuki reactions .
| Entry | R | Z | X | Time (min) | Yield (%) | TON | TOF |
|---|---|---|---|---|---|---|---|
| 1 | H | Styrene | Br | 120 | 94 | 9400 | 4700 |
| 2 | H | Styrene | Cl | 150 | 79 | 7900 | 3160 |
| 3 | H | Styrene | I | 120 | 96 | 9600 | 4800 |
| 4 | 4–Me | Styrene | Br | 120 | 90 | 9000 | 4500 |
| 5 | 4–Me | Styrene | Cl | 150 | 75 | 7500 | 3000 |
| 6 | 4–Me | Styrene | I | 120 | 94 | 9400 | 4700 |
| 7 | 4–OMe | Styrene | Br | 120 | 91 | 9100 | 4550 |
| 8 | 4–OMe | Styrene | I | 120 | 93 | 9300 | 4650 |
| 9 | 4–NMe2 | Styrene | Br | 120 | 93 | 9300 | 4650 |
| 10 | 4–Cl | Styrene | Br | 120 | 96 | 9600 | 4800 |
| 11 | 4–Cl | Styrene | Cl | 150 | 70 | 8000 | 3200 |
| 12 | 4–CN | Styrene | Br | 120 | 94 | 9400 | 4700 |
| 13 | 4–CN | Styrene | Cl | 150 | 78 | 8800 | 3520 |
| 14 | 4–CHO | Styrene | Br | 120 | 93 | 9300 | 4650 |
| 15 | H | butyl acrylate | Br | 120 | 96 | 9600 | 4800 |
| 16 | H | butyl acrylate | Cl | 150 | 82 | 8200 | 3280 |
| 17 | H | butyl acrylate | I | 90 | 96 | 9600 | 6400 |
| 18 | 4–Me | butyl acrylate | Br | 120 | 89 | 8900 | 4450 |
| 19 | 4–Me | butyl acrylate | Cl | 150 | 75 | 7500 | 3000 |
| 20 | 4–OMe | butyl acrylate | Br | 120 | 91 | 9100 | 4550 |
| 21 | 4–OMe | butyl acrylate | Cl | 150 | 76 | 7600 | 3040 |
| 22 | 4–CN | butyl acrylate | Br | 120 | 94 | 9400 | 4700 |
| 23 | 4–CN | butyl acrylate | Cl | 150 | 89 | 8900 | 3560 |
| 24 | H | Ph(BOH)2 | Br | 120 | 92 | 9200 | 4600 |
| 25 | H | Ph(BOH)2 | I | 150 | 97 | 9700 | 3880 |
| 26 | 4–Me | Ph(BOH)2 | Br | 120 | 88 | 8800 | 4400 |
| 27 | 4–Me | Ph(BOH)2 | I | 150 | 92 | 9200 | 3680 |
| 28 | 4–OMe | Ph(BOH)2 | Br | 120 | 84 | 8400 | 4200 |
| 29 | 4–Cl | Ph(BOH)2 | Br | 120 | 93 | 9300 | 4650 |
| 30 | 4–CN | Ph(BOH)2 | Br | 120 | 95 | 9500 | 4750 |
| 31 | 4–CN | Ph(BOH)2 | I | 150 | 99 | 9900 | 3960 |
| 32 | H | Styrene | I | 120 | 85 | 8500 | 4250 |
| 33 | H | Ph(BOH)2 | I | 120 | 83 | 8300 | 4150 |
Reaction conditions: styrene, butyl acrylate, or phenylboronic acid (1 mmol); phenyl halide (1 mmol); Pd@Py2PZ@MSN catalyst (1 mol%); H2O (5 ml); TEA (1.5 mmol); 25°C.
TON is calculated as the number of moles of the substrate converted to the product divided by the number moles of palladium catalyst.
TOF is defined as TON h−1.
Scale-up reactions: styrene or phenylboronic acid (10 mmol); phenyl bromide (10 mmol); Pd@Py2PZ@MSN catalyst (1 mol%); H2O (50 ml); TEA (15 mmol); 25°C.
SCHEME 2Proposed mechanism for Pd@Py2PZ@MSN catalyzed carbon–carbon bond formation.
FIGURE 3Recovery results of the Pd@Py2PZ@MSN catalyst.
FIGURE 4SEM image of the recovered Pd@Py2PZ@MSN catalyst.
Surface area and pore size results of the recovered Pd@Py2PZ@MSN catalyst.
| Surface area (m2.g−1) | Pore width (nm) | Pore volume (cm3.g−1) |
|---|---|---|
| 607.21 | 5.09 | 0.70 |
Comparison of the catalytic activity of Pd@Py2PZ@MSN with the previously reported one.
| Entry | Catalyst | Conditions | Time (h) | Yields |
|---|---|---|---|---|
| 1 | Pd/TiO2 NP | DMF, Et3N, 140°C | 10 | 93 |
| 2 | Pd/SMNPs-DF | Solvent free, DABCO, 140°C | 0.9 | 93 |
| 3 | CO-NHC@MWCNTs | PEG, Li2CO3, 80°C | 10 | 67 |
| 4 | Pd/MPCS-TI | DMF/H2O, Et3N, 110°C | 4 | 93 |
| 5 | Pd/BIP-silica-Fe2O3 | DMF, Et3N, 100°C | 3.5 | 82 |
| 6 | Pd/Guanidine/graphene | EtOH/H2O, K2CO3, r.t. | 2 | 92 |
| 7 | This work | H2O, TEA, 25°C | 1 | 94 |
Isolated yields.