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

Table 4. Ethylene Polymerization of C1 at 0–80 °Ca.

entry temp (°C) time (min) yield (g) productivity (kg mol–1Ni h) TOF (103)(h–1) Mnb (kg mol–1) Đb Tmc (°C) B/1000Cd branching distribution (%)f
Me Et Pr Bu Am Lg
1 0 30 1.1 440 15.7 65.1 1.65 127.8 5 100 0 0 0 0 0
2 20 10 2.4 2880 102.9 11.4 1.93 108.6 25 94.3 3.5 2.2 0 0 0
3 40 10 1.8 2160 77.1 3.7 1.66 64.4 56(46)e 80.0 4.7 2.9 2.6 2.1 7.6
4 60 10 2.2 2640 94.3 2.0 1.51 9.3 95(72)e 74.0 6.2 4.1 2.6 3.4 9.7
5 80 10 0.7 840 30.0 1.0 1.74 –23.6 127(81)e 66.4 7.5 4.5 2.8 6.6 12.1
a

Conditions: 5 μmol of Ni catalyst, 10 equiv of B(C6F5)3, 400 psi ethylene, 45 mL of toluene.

b

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

c

Determined by differential scanning calorimetry.

d

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

e

Branching density corrected for saturated end groups.

f

Determined by 13C NMR in D2-tetrachloroethane at 125 °C. Percentages of branch length determined from relative intensity ratios of methyl (1B1, 1B2, 1B3), methylene (2B4, 3B5) or methine (brB4+) signals of the respective branch. TOF = Turnover Frequency, Mn = Number-Average Molecular Weight, Đ = Dispersity, Tm = Melting Temperature, Me = Methyl, Et = Ethyl, Pr = Propyl, Bu = Butyl, Am = Amyl, Lg = Large.