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. 2024 Aug 16;14(17):13136–13147. doi: 10.1021/acscatal.4c02708

Table 2. Ethylene Polymerization of C1–C8 at 20 °Ca.

entry catalyst time (min) yield (g) productivity (kg mol–1Ni h) TOF (103)(h–1) B/1000Cb Mnc (kg mol–1) Đc Tmd (°C)
1e C1 10 2.4 2880 102.9 25 11.4 1.93 108.6
2 C3 10 1.7 1020 36.4 30 7.8 1.94 101.0
3 C5 10 1.6 960 34.3 37 11.7 1.97 99.7
4 C7 10 0.8 480 16.8 26 153.7 1.77 101.5
5e C2 60 1.5 300 10.7 36 6.9 1.92 102.1
6 C4 60 0.9 90 3.2 49 23.8 1.75 112.0
7 C6 60 1.2 120 4.3 45 37.0 1.62 82.9
8 C8 180 0.5 167 0.6 42 71.3 2.06 91.5
a

Conditions: 10 μmol of Ni catalyst, 10 equiv of B(C6F5)3, 400 psi ethylene, 45 mL of toluene.

b

Determined by 1H NMR in D2-tetrachloroethane at 125 °C.

c

Determined by GPC in 1,2,4-trichlorobenzene at 160 °C using polystyrene calibration.

d

Determined by differential scanning calorimetry.

e

5 μmol of Ni. TOF = Turnover Frequency, Mn = Number-Average Molecular Weight, Đ = Dispersity, Tm = Melting Temperature.