ADMET polymerization of M1 using G2 in the presence of cross-linker (CL)a.
Run | CLb/mol% | Time/h | M n c | M w/Mnc | Yieldd/% |
---|---|---|---|---|---|
8 | — | 12 | 12 700 | 1.85 | 91 |
21 | 2.5 | 12 | 13 300 | 2.58 | 88 |
22 | 2.5 | 18 | 13 600 | 2.28 | 89 |
23 | 5.0 | 12 | 11 500 | 3.95 | 88 |
24 | 5.0 | 18 | 13 500 | 3.48 | 88 |
25e | 5.0 | 18 | 13 800 | 2.80 | 90 |
26f | 5.0 | 18 | 10 200 | 2.05 | 81 |
27f | 5.0 | 24 | 11 800 | 2.59 | 86 |
Conditions: monomer M1 (330 mg, 1.0 mmol), ruthenium catalyst (G2) 1.5 mol%, cross-linker (CL), CH2Cl2 0.4 mL (initial monomer concentration 2.50 M), 50 °C. Detailed procedure is shown in the Experimental section.
Mol% based on monomer M1.
GPC data in THF vs. polystyrene standards.
Isolated yield by precipitation as the methanol insoluble fraction.
Ru 2.0 mol%.
Cross-linker (CL, 5.0 mol%) was added after 30 min.