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. 2022 Feb 17;28(14):e202104198. doi: 10.1002/chem.202104198

Table 2.

NA/CHO ROCOP data using catalysts 18 and compared against leading catalysts from the literature (See Figure 1 for reaction scheme).[a]

Entry

[LMg(II)M(II)(OAc)2] M, cat #

Conv. [%][b]

Polymer [%][c]

TON[d]

TOF [h−1][e]

k p′ [mM−1 s−1][f]

k rel[g]

M n [kg mol−1] [Ð][h]

1

Mg, 1

>99

>99

100

71 (±4)

8.7 (±0.5)

1.0

1.6 [1.15]

2

Cr, 2

>99

>99

100

54 (±3)

6.6 (±0.4)

0.8

n.d

3

Mn, 3

>99

>99

100

272 (±13)

33.5 (±1.6)

3.9

1.4 [1.14]

4

Fe, 4

>99

>99

100

109 (±5)

13.4 (±0.6)

1.5

1.3 [1.15]

5

Co, 5

>99

>99

100

610 (±31)

75.2 (±3.8)

8.6

1.5 [1.14]

6

Ni, 6

>99

>99

100

244 (±12)

30.1 (±1.5)

3.5

1.4 [1.15]

7

Cu, 7

>99

>99

100

170 (±9)

21.2 (±1.1)

2.4

1.2 [1.15]

8

Zn, 8

>99

>99

100

186 (±10)

23.0 (±1.2)

2.6

1.3 [1.14]

9[i][52]

(ONSO)CrCl/PPNCl

97

>99

243

360

11.9 [1.28]

10[j][50]

(salophen)CrCl/DMAP

97

>99

243

49

3.0 [1.12]

11[k][13a]

(salen[CyPr]+)AlCl2

51

>99

204

34

8.2 [1.24]

12[l][53]

(o‐van)AlK(OAc)2

33

>99

133

266

4.5 [1.10]

13[m]

Co

>99

>99

100

666 (±21)

2.2 [1.14]

[a] Reaction conditions: [cat]0:[CHD]0:[NA]0:[CHO]0=1 : 20 : 100 : 2000; 0.05 mol% catalyst loading (4.88 mM), 20 equivalents trans‐1,2‐cyclohexendiol (97.6 mM), neat CHO (3.2 mL, 9.9 M), 100 °C. [b] Expressed as a percentage of epoxide conversion against the theoretical maximum (100 %). [c] Expressed as a percentage of polymer selectivity against cyclic carbonate formation. [d] Turn over number (TON)=number of moles of monomer converted/number of moles of catalyst. [e] Turn over frequency (TOF)=TON/hour. [f] k p=rate coefficient=k obs/[cat]1 where k obs is calculated from the gradient of the plot of [NA] vs. time (s). [g] k rel=relative rate coefficient=k p(MgM)/k p(MgMg). [h] Determined by SEC analysis, in THF, calibrated with narrow‐M n polystyrene standard; dispersity values in parentheses. [i] Reaction conditions: [cat]0/[PPNCl]0:[NA]0:[CHO]0=1 : 1 : 250 : 250 in toluene (2 mL), 110 °C. [j] Reaction conditions: [cat]0:[DMAP]0:[NA]0:[CHO]0=1 : 1 : 250 : 250 in toluene, 110 °C. [k] Reaction conditions: [cat]0:[NA]0:[CHO]0=1 : 400 : 2000, 0.05 mol % catalyst loading, neat CHO (9.9 M), 60 °C. [l] Reaction conditions: [cat]0:[NA]0;[CHO]0=1 : 400 : 2000, 0.05 mol %, neat CHO (9.9 M), 100 °C. [m] Reaction with Phthalic Anhydride (PA). For reported catalyst structures, entries 9–13, see Figure S31.