Development of Covalent Triazine Frameworks as Heterogeneous Catalytic Supports
Abstract
:1. Introduction to Covalent Triazine Frameworks (CTFs)
2. Design and Synthesis Methods of CTFs
2.1. Trimerization of Aromatic Nitriles
2.2. Polycondensation Synthesis Route
2.3. Cross-Coupling of Triazine-based Building Blocks
2.4. Characterization of CTFs
3. CTFs as Support for Heterogeneous Catalysis
3.1. Support for Metal Nanoparticles
3.2. Immobilization of Molecular Metal Catalysts
4. Conclusions and Outlook
Funding
Acknowledgments
Conflicts of Interest
References
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Material | Monomer | Metal content | Type of Reaction | Activity | Ref |
---|---|---|---|---|---|
Pd/CTF | 1 wt % Pd (nanoparticles) | Oxidation of glycerol into glyceric acid | Rate of glycerol mol·h−1·mol−1 consumption: 982 Selectivity = 81% | [28] | |
Pd/CTF | 1 wt % Pd (nanoparticles) | Oxidation of Benzyl alcohol | Turn-over frequency (TOF) = 1453 h−1 Selectivity = 98% | [30] | |
Pd/CTF | 4 wt % Pd (nanoparticles) | Hydrogenation of N-heterocycles (1,10-phenanthroline) | Pressure/Selectivity = 30 bar/98.9%; 20 bar/97.9% for 8H-phen TOF = 47.6 h−1 (1st cycle) | [32] | |
Pd/CTF | 2.05 wt % Pd (nanoparticles) | Selective double carbonylation of aryl iodides | Several substrates tested Yield up to 90% with selectivity = 95% | [33] | |
Ru/CTF-c | 3.91 wt % Ru (nanoparticles) | Oxidation of 5-hydroxymethylfurfural to 2,5-furandicarboxylic acid | Conversion > 99% Yield = 41.4% | [35] | |
Ru/CTF-c | 5 wt % Ru coordination using (RuCl2(p-cymene))2 | Hydrogenolysis of xylitol | Full conversion with 15% selectivity to propylene glycol | [36] | |
CTF-DCE-Ag | 4.3 wt % Ag (nanoparticles) | Carboxylation of terminal alkynes | TON: 247 Yield > 98.9 | [37] | |
Pt-CTF | - | Low temperature oxidation of methane to methanol | Selectivity > 75% TON = 246 | [38] | |
Ir@CTF | 2.4 wt % Ir | Isomerization of 1-octen-3-ol to 3-octanone | TOF = 24 min−1 | [40] | |
Rh@CTF-c | 3.5 wt % Rh | Hydroformylation of crude 1-octene | 62% conversion TOF = 600h−1 TON = 12,000 | [42] | |
CTF-Ir | 16 wt % Ir | Dehydrogenation of formic acid | TOF = 27,000 h−1 TON = 1,060,000 | [43] | |
Ir@meso-CTF | 2 wt % Ir | Hydrogenation of CO2 | TON = 358 | [44] | |
Ir@meso-CTF@monolith | 0.23 μmol/0.045 mg Ir | Dehydrogenation of formic acid | TOF = 207,200 h−1/TON = 2230 | [45] | |
Bpy-CTF-(IrCp*Cl)Cl | 4.7 wt % Ir | Hydrogenation of CO2 to formate | TOF = 5300 h−1 TON = 5000 | [47] | |
(bpy-CTF-Ru(acac)2)Cl | 1.68 wt % Ru | Hydrogenation of CO2 to formate | TOF = 22,700 h−1 TON = 21,200 | [48] | |
(bpy-CTF-RuCl3) | 2.1 wt % Ru | Hydrogenation of CO2 to formate | TOF = 38,800 h−1 TON = 20,000 | [49] | |
(bpy-CTF(RhCp*Cl)Cl) &(bpy-CTF(IrCp*Cl)Cl) | 1.78 wt % Rh & 4.7 wt % Ir | Transfer hydrogenation of carbonyl compounds | Conversion = 99% Rh catalyst is more active than Ir catalyst. But, only Ir catalyst maintained activity during recycling. | [50] | |
(bpy-CTF-Al(OTf)2) (Co(CO)4) | 3.76 wt % Al & 2.67 wt % Co | Carbonylation of epoxides into β-lactones | Conversion > 99% Selectivity = 90% | [51] | |
Ir(I)@bipyCTF | 8.26 wt % Ir | C-H borylation of 1,2-dichlorobenzene | TON = 64 Yield = 95% | [52] | |
Ir0.68-NHC-CTF | 0.68 wt % Ir | Hydrogenation of CO2 to formate | TOF = 1600 h−1 TON = 24,300 | [53] | |
Rh-bpim-CTF | 0.61 wt % Rh | Carbonylation of methanol | Conversion = 93% TOF = 2100 h−1 | [54] | |
(imidazolium-CTF)(Co(CO)4) | 3.62 wt % Co | Direct Synthesis of Methyl 3-Hydroxybutyrate from Propylene Oxide | Conversion > 99% Selectivity = 86% | [55] | |
V@acacCTF | 1.6 wt % V | Mannich reaction between 2-naphthol and N-methylmorpholine N-oxide | TON = 213 Conversion = 100% Yield = 95% | [57] |
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Tahir, N.; Krishnaraj, C.; Leus, K.; Van Der Voort, P. Development of Covalent Triazine Frameworks as Heterogeneous Catalytic Supports. Polymers 2019, 11, 1326. https://doi.org/10.3390/polym11081326
Tahir N, Krishnaraj C, Leus K, Van Der Voort P. Development of Covalent Triazine Frameworks as Heterogeneous Catalytic Supports. Polymers. 2019; 11(8):1326. https://doi.org/10.3390/polym11081326
Chicago/Turabian StyleTahir, Norini, Chidharth Krishnaraj, Karen Leus, and Pascal Van Der Voort. 2019. "Development of Covalent Triazine Frameworks as Heterogeneous Catalytic Supports" Polymers 11, no. 8: 1326. https://doi.org/10.3390/polym11081326
APA StyleTahir, N., Krishnaraj, C., Leus, K., & Van Der Voort, P. (2019). Development of Covalent Triazine Frameworks as Heterogeneous Catalytic Supports. Polymers, 11(8), 1326. https://doi.org/10.3390/polym11081326