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. Author manuscript; available in PMC: 2014 May 3.
Published in final edited form as: Angew Chem Int Ed Engl. 2013 Apr 8;52(19):10.1002/anie.201300293. doi: 10.1002/anie.201300293

Table 1.

Polymerization of monomer 3a using ROMP

entry [M]o/[I] catalyst solvent[a] temp
(°C)
time
(h)
conversion
(%)[b]
Yield[c,d] Mntheo
(g/mol)
MnNMR [e]
(g/mol)
MnGPC [f]
(g/mol)
PDI[f]
(Mn/Mw)
1 100/1 GII CHCl3 20 4 84 72 23600 103800 63200 2.8
2 100/1 GII CHCl3 45 18 81[g] 49 22800 26000 24900 2.6
3 25/1 5 THF 20 1 87 57 6100 6500 9300 1.4
4 50/1 5 THF 20 1 85 71 12000 12500 16300 1.4
5 100/1 5 THF 20 1 81 80 23100 22000 21600 1.4
6 100/1 5 THF 20 18 81 85 23100 22100 22300 1.4
7 200/1 5 THF 20 1 73 83 41000 45200 50300 1.5
[a]

[M]o = 1M.

[b]

based off of 1H-NMR integrations of monomer olefin signals to polymer olefin signals.

[c]

isolated.

[d]

theoretical yield based off of monomer conversion.

[e]

based off 1H-NMR integrations of polymers olefin signals and polymers chain-end phenyl signals.

[f]

calibrated with polystyrene standards, eluted in THF,

[g]

additional 10–15% cyclic dimer (see Supporting Information for structural characterization of byproduct).