2021
DOI: 10.1002/mats.202100024
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Exploiting (Multicomponent) Semibatch and Jacket Temperature Procedures to Safely Tune Molecular Properties for Solution Free Radical Polymerization of n‐Butyl Acrylate

Abstract: Free radical polymerization (FRP) of acrylates is under conventional lab‐scale batch conditions characterized by strong nonisothermicity. Hence, side reactions with a high activation energy such as β‐scission are highly relevant already at intermediate temperatures (313–333 K), broadening the log‐molar mass distribution and decreasing the average molar masses. To avoid thermal runaway, one can design jacket temperature profiles or exploit semibatch reactor operations. Model‐based design with stochastic solvers… Show more

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Cited by 9 publications
(3 citation statements)
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“…Model-based design for acrylate radical polymerization is also possible upon considering step-wise T j variations and semibatch operation, as recently demonstrated under FRP conditions. ,, In the present work, this is further illustrated under NMP conditions in ( i ) Figure a–f, considering three variable T j profiles, with temperature variations between 383 and 403 K, and with three flat counter cases with fixed T j values of 383, 393, and 403 K, and in ( ii ) Figure a–f, considering three semibatch profiles with nitroxide and one batch counter case.…”
Section: Resultsmentioning
confidence: 99%
“…Model-based design for acrylate radical polymerization is also possible upon considering step-wise T j variations and semibatch operation, as recently demonstrated under FRP conditions. ,, In the present work, this is further illustrated under NMP conditions in ( i ) Figure a–f, considering three variable T j profiles, with temperature variations between 383 and 403 K, and with three flat counter cases with fixed T j values of 383, 393, and 403 K, and in ( ii ) Figure a–f, considering three semibatch profiles with nitroxide and one batch counter case.…”
Section: Resultsmentioning
confidence: 99%
“…Gradient structures (in controlled radical polymerizations) or compositional drift (in free-radical polymerizations) emerge when one reactivity ratio is >1 and the other <1, with the monomer having the larger reactivity ratio being consumed first. Previous studies have used Monte Carlo simulations to examine copolymer sequences based on reactivity ratios. This methodology can be extended to model fragment sizes post-degradation in the context of the CC approach. For example, we conducted simulations involving 2.5% CC loading with a degree of polymerization (DP) of 1000 and plotted the weight-average molar mass ( M w ) of the oligomeric fragments obtained after CC cleavage relative to the M w of the starting copolymer under various reactivity ratio scenarios (Figure A; see Supporting Information for simulation details). The use of M w for plotting conveys information about the largest fragments, which is important for assessing the performance of CCs.…”
Section: Introductionmentioning
confidence: 99%
“…Knowledge of acrylate polymerization kinetics has continued to evolve, as summarized in a review by Ballard and Asua . In particular, backbiting, MCR migration, Beta-Scission, and its effect on the average molar mass and microstructure have been investigated. The kinetics of polymerization of acrylate monomers has been studied by different research groups. ,,, Numerous advancements have been made in this regard, particularly through the use of electron spin resonance (ESR) spectroscopy and pulsed laser polymerization (PLP) methods. ,,, Different methodologies have been used to report rate coefficients for various reactions, , ,,, e.g., Beta-Scission, ,, chain transfer to solvent, ,, termination of secondary radicals, ,, and termination of tertiary radicals. , …”
Section: Introductionmentioning
confidence: 99%