The mechanism of atom transfer radical polymerization (ATRP) mediated by sodium dithionite (Na 2 S 2 O 4 ), with Cu II Br 2 /Me 6 TREN as catalyst (Me 6 TREN: tris[2-(dimethylamino)ethyl]amine) in ethanol/water mixtures, was investigated experimentally and by kinetic simulations. A kinetic model was proposed and the rate coefficients of the relevant reactions were measured. The kinetic model was validated by the agreement between experimental and simulated results. The results indicated that the polymerization followed the SARA ATRP mechanism, with a SO 2 ˙ − radical anion derived from Na 2 S 2 O 4 , acting as both supplemental activator (SA) of alkyl halides and reducing agent (RA) for Cu II /L to regenerate the main activator Cu I /L. This is similar to the reversible-deactivation radical polymerization (RDRP) procedure conducted in the presence of Cu 0 . The electron transfer from SO 2 ˙ − , to either Cu II Br 2 /Me 6 TREN or R–Br initiator, appears to follow an outer sphere electron transfer (OSET) process. The developed kinetic model was used to study the influence of targeted degree of polymerization, concentration of Cu II Br 2 /Me 6 TREN and solubility of Na 2 S 2 O 4 on the level of polymerization control. The presence of small amounts of water in the polymerization mixtures slightly increased the reactivity of the Cu I /L complex, but markedly increased the reactivity of sulfites.
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Two-compartment kinetic Monte Carlo modelling of electrochemically mediated ATRP
For electrochemically mediated atom transfer radical polymerization (eATRP), novel mechanistic insights are formulated based on a two-compartment kinetic Monte Carlo model in which catalyst concentration gradients between a large “bulk” compartment away from the electrode and a very small compartment around the electrode are accounted for to reflect the concept of the Nernst diffusion layer. The mass transport of deactivator catalyst to the electrode and its electrochemical reduction at the electrode are treated separately to enable the model to explicitly distinguish between limitations of mass transport and limitations due to intrinsic chemical reactivity. The model is applied to eATRP of methyl acrylate at 298 K with Cu II Br 2 /Me 6 TREN (Me 6 TREN: tris((2-dimethylamino)ethyl)amine) and eATRP of n -butyl acrylate at 317 K with Cu II Br 2 /TPMA (TPMA: tris(2-pyridylmethyl)amine). Diffusional limitations on termination need to be accounted for to properly reflect the eATRP kinetics and the microstructural properties of the obtained polymers. In most cases, an eATRP with mixed chemical and mass transport control is obtained.
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- Award ID(s):
- 1707490
- PAR ID:
- 10184889
- Date Published:
- Journal Name:
- Reaction Chemistry & Engineering
- Volume:
- 3
- Issue:
- 6
- ISSN:
- 2058-9883
- Page Range / eLocation ID:
- 866 to 874
- Format(s):
- Medium: X
- Sponsoring Org:
- National Science Foundation
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