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Maps copolymerization curves in a polymer system, suggesting improved data efficiency through innovative methods.
High Resolution Image Download MS PowerPoint Slide Copolymerization curves and reactivity-ratio estimates are traditionally derived from sparse offline data collected across many separate experiments. Here, we propose a data-efficient workflow for apparent finite-conversion reactivity-ratio estimation that combines gradient continuous-flow free-radical copolymerization, inline ATR-FTIR spectroscopy, and sparse linear regression to reconstruct dense concentration and composition trajectories from minimal offline quantitation. Using styrene/methyl methacrylate as a benchmark system, we performed a time-programmed zigzag sweep of the styrene/MMA feed ratio at constant total flow and acquired more than 700 inline ATR-FTIR spectra in a single ∼4 h run at each of 70, 80, and 90 °C. Only ten offline UHPLC anchor points per run were used to calibrate Lasso models for monomer concentration prediction, enabling high-density reconstruction of the reference monomer composition f 1 ( t ), total conversion X tot ( t ), and cumulative consumption-based copolymer-composition proxy F 1,cum ( t ). The reconstructed finite-conversion trajectories were analyzed using a Skeist-type finite-conversion terminal-model formulation, in which the Mayo–Lewis equation was used as the instantaneous composition relation. The maximum X tot values spanned 0.36–0.62, and the full-data IR-assisted estimates spanned r 1 = 0.33–0.48 and r 2 = 0.39–0.44, remaining within the broad range of benchmark literature values for this system. Residual-based Monte Carlo sampling showed that pointwise concentration-prediction uncertainty led to compact r 1 – r 2 ensembles, whereas block-removal and UHPLC-only subset analyses revealed sensitivity to sparse-anchor selection, most notably at 70 °C. Because the workflow uses finite-conversion trajectory data, aligned reference/reacting concentration differences, and this F 1,cum proxy, the reported values are interpreted as apparent finite-conversion estimates under the present flow and analysis workflow. This approach provides a practical route to dense, uncertainty-aware copolymerization-trajectory mapping from minimal offline measurements and enables unified comparison of apparent finite-conversion reactivity-ratio estimates across temperatures.
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Wakiuchi et al. (2026) studied this question.
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