| Literature DB >> 35944187 |
Maria Voccia1, Lukas Odenwald2, Maximilian Baur2, Fei Lin2, Laura Falivene1, Stefan Mecking2, Lucia Caporaso1.
Abstract
Polyethylene materials with in-chain-incorporated keto groups were recently enabled by nonalternating copolymerization of ethylene with carbon monoxide in the presence of Ni(II) phosphinephenolate catalysts. We elucidate the mechanism of this long-sought-for reaction by a combined theoretical DFT study of catalytically active species and the experimental study of polymer microstructures formed in pressure-reactor copolymerizations with different catalysts. The pathway leading to the desired nonalternating incorporation proceeds via the cis/trans isomerization of an alkyl-olefin intermediate as the rate-determining step. The formation of alternating motifs is determined by the barrier for the opening of the six-membered C,O-chelate by ethylene binding as the decisive step. An η2-coordination of a P-bound aromatic moiety axially oriented to the metal center is a crucial feature of these Ni(II) catalysts, which also modulates the competition between the two pathways. The conformational constraints imposed in a 2',6'-dimethoxybiphenyl moiety overall result in a desirable combination of disfavoring ethylene coordination along the alternating incorporation pathway, which is primarily governed by electronics, while not overly penalizing the nonalternating chain growth, which is primarily governed by sterics.Entities:
Year: 2022 PMID: 35944187 PMCID: PMC9413223 DOI: 10.1021/jacs.2c04563
Source DB: PubMed Journal: J Am Chem Soc ISSN: 0002-7863 Impact factor: 16.383
Chart 1Ni(II) Phosphinephenolate Catalysts Studied, and Phosphinesulfonato Pd(II) Reference System
Polymerization Resultsa
| cat. | yield [mg] | TOF | χNMR | microstr. I/NA/A | insertions na/alt |
|---|---|---|---|---|---|
| 34 | 1.46 | 7.3 | 82:17:1 | 92:8 | |
| 11 | 0.47 | 10.3 | 34:51:15 | 60:40 | |
| 25 | 1.07 | 8.4 | 56:39:5 | 75:25 | |
| 37 | 1.59 | 10.8 | 19:51:30 | 45:55 | |
| 31 | 1.33 | 14.4 | 19:53:28 | 46:54 | |
| 12 | 0.51 | 36.7 | 0:18:82 | 9:91 |
Reaction conditions: 10 μmol catalyst precursor, 200 mL of toluene 90 °C, 0.02 bar 13CO, 5 min reaction time, 10 bar reaction pressure, and 1000 rpm (cf. SI for the polymerization procedure).
TOF given in units of 103 mol[C2H4] mol–1[Ni] h–1.
Determined by 1H-NMR spectroscopy.
I: isolated carbonyl, NA: nonalternating motifs, A: alternating motifs. Determined by 13C NMR spectroscopy (Figure S9) according to ref (20).
Relative ratio of nonalternating and alternating carbon monoxide incorporation events, derived from the microstructure ((I + 0.5 NA)/(0.5 NA + A)).
Figure 1Geometries of the chelate 1-cycle5-T intermediate for catalysts 1 (left) and 2 (right). Distances are in Å.
Figure 2Free energies (ΔGtol in kcal/mol) of the key steps for nonalternating and alternating carbon monoxide incorporation with catalysts 1 (red) and 2 (blue). The labels of the species in black (intermediates and TSs) refer to 1-* for species involved in monomer incorporation (E or CO) from 1-cycle5-T, 2-* for the next (second) monomer (CO + E) incorporation.
Figure 3Topographic steric maps of the transition state TS for catalysts 1 (top left) and 2 (top right). The complexes are oriented as shown below (bottom left and right).[30]
Figure 4Geometry of TS-1 for catalysts 1 (left) and 2 (right). Distances are reported in Å.
Figure 5Topographic steric maps of transition state TS for catalysts 2 (left), 3 (in the center), and 4 (right). The Ni···Cipso distances are reported in Å.
Figure 6Topographic steric maps of TS for catalysts 2 (left) and 2′ (right).