Table 1.
Entry | fGB:POa | FGB:POb | TOF (h−1)c | Selectivity (%)d | Tg °Ce | Mn (kg/mol)f | Ð (Mw/Mn)f |
---|---|---|---|---|---|---|---|
PGBC-100 | 100:0 | 100:0 | 74 | 85 | −7 | 12.4 | 1.20 |
PPGBC-87 | 90:10 | 87:13 | 78 | 86 | −30 | 6.1 | 1.12 |
PPGBC-74 | 70:30 | 74:26 | 129 | 82 | −29 | 6.0 | 1.10 |
PPGBC-56 | 50:50 | 56:44 | 144 | 95 | −9 | 8.6 | 1.08 |
PPGBC-33 | 30:70 | 33:67 | 158 | 90 | −12 | 13.6 | 1.11 |
PPGBC-22 | 10:90 | 22:78 | 225 | 99 | 0 | 9.6 | 1.11 |
PPC-100 | 0:100 | 0:100 | 444 | >99 | 28 | 22 | 1.18 |
The reaction was performed in neat epoxide (10 mmol) in a 15 mL autoclave under 2.7 MPa CO2 pressure at 40 °C with 2000:1 catalyst loading
aMolar ratio of monomer feed
bMolar ratio of monomer incorporation in polymer chain
cTurnover frequency (TOF) = mole of product (polycarbonates)/mol of cat. per hour. Reactions were stopped at ~60% conversion
dPercent of polymer formed vs. cyclic carbonate as determined by 1H NMR
eDetermined by DSC analysis
fDetermined by gel permeation chromatography in THF, calibrated with polystyrene standards