The successful application of poly(N-vinylcaprolactam)-based microgels requires a profound understanding of their synthesis. For this purpose, a validated process model for the microgels synthesis by precipitation copolymerization with the cross-linker N,N′-methylenebis-(acrylamide) is formulated. Unknown reaction rate constants, reaction enthalpies, and partition coefficients are obtained by quantum mechanical calculations. The remaining parameter values are estimated from reaction calorimetry and Raman spectroscopy measurements of experiments with different monomer/cross-linker compositions. Because of high crosspropagation reaction rate constants, simulations predict a fast incorporation of the cross-linker. This agrees with reaction calorimetry measurements. Furthermore, the gel phase is predicted as the major reaction locus. The model is utilized for a prediction of the internal particle structure regarding its crosslink distribution. The highly cross-linked core reported in the literature corresponds to the predictions of the model.
Reversible addition−fragmentation chain transfer (RAFT) copolymerizations of methacrylic acid Nhydroxysuccinimide ester and cyclic N-vinylamide derivatives (N-vinylpyrrolidone, N-vinylpiperidone, and N-vinylcaprolactam) were successfully performed with methyl 2-(ethoxycarbonothioylthio)propanoate as chain transfer agent (CTA). Effects of different reaction parameters, such as solvent type, temperature, and CTA-to-initiator (C/I) ratio, were studied to optimize the polymerization conditions in order to obtain copolymers with variable chemical composition, controlled molecular weight, and narrow polydispersity index (PDI). The solvent type has a high impact on the polymerization reaction, and a high C/I ratio decreases polydispersity as well as conversion. Increased steric hindrance through an enlarged lactam ring offsets the monomer reactivity. The controlled character of RAFT polymerization was evidenced by the low PDI of the copolymers and a linear relationship between conversion and molecular weight. Biohybrid nanogels were synthesized by direct coupling between reactive copolymers and enhanced green fluorescent protein (EGFP) or cellulase (CelA2_M2) at room temperature in a water-in-oil emulsion. The EGFP-conjugated nanogels were fluorescent, while the CelA2_M2 encapsulated in nanogels retained its catalytic activity, as demonstrated by the hydrolysis of 4-methylumbelliferyl-β-D-cellobioside.
Microgels are commonly synthesized in batch experiments, yielding quantities sufficient to perform characterization experiments for physical property studies. With increasing attention on the application potential of microgels, little attention is yet paid to the questions (a) whether they can be produced continuously on a larger scale, (b) whether synthesis routes can be easily transferred from batch to continuous synthesis, and (c) whether their properties can be precisely controlled as a function of synthesis parameters under continuous flow reaction conditions. We present a new continuous synthesis process of two typical but different microgel systems. Their size, size distribution, and temperature-responsive behavior are compared in depth to those of microgels synthesized using batch processes, and the influence of premixing and surfactant is also investigated. For the surfactant-free poly( N-vinylcaprolactam) and poly( N-isopropylacrylamide) systems, microgels are systematically smaller, while the actual size is depending on the premixing of the reaction solutions. However, by the use of a surfactant, the size difference between batch and continuous preparation diminishes, resulting in equal-sized microgels. Temperature-induced swelling-deswelling of microgels synthesized under continuous flow conditions was similar to that of their analogues synthesized using the batch polymerization process. Additionally, investigation of the internal microgel structure using static light scattering showed no significant changes between microgels prepared under batch and continuous conditions. The work encourages synthesis concepts of sequential chemical conditions in continuous flow reactors to prepare precisely tuned new microgel systems.
This contribution presents in-line monitoring of microgel synthesis by precipitation polymerization based on Raman spectroscopy. The spectra are evaluated via multivariate Indirect Hard Modeling (IHM) regression. Therefore, mechanistic models of the pure component spectra for solvent, monomer, and microgel are created by a sum of adaptable parameterized peak functions (Gaussian-Lorentzian). Instead of individual calibrations for each analyte, one comprehensive model is calibrated to predict both the monomer and microgel fraction while ensuring a consistent mass balance. As a novelty, this leads to an in-line microgel quantification based on an interactive spectral model. The results show cross-validation errors (RMSECV) of monomer and microgel fractions as low as 0.028 wt % and 0.084 wt %, respectively. The ability of IHM to account for non-linear spectral changes was found to reduce the microgel RMSECV by a factor of two compared to linear CLS regression. The calibration model allows simultaneous observation of the decrease in monomer content and the formation of microgels. Long as well as short focus immersion optics reveal characteristic vibrations of the turbid microgel suspension, although long focus optics are influenced by scattering particles to a greater extent. Precise examination of the model proves that the prediction is robust against changes in microgel particle size or temperature, which opens up the application of Raman spectroscopy as a comprehensive process analytical technology in microgel synthesis.
Poly(
N
-isopropylacrylamide) microgels have found various uses
in fundamental polymer and colloid science as well as in different
applications. They are conveniently prepared by precipitation polymerization.
In this reaction, radical polymerization and colloidal stabilization
interact with each other to produce well-defined thermosensitive particles
of narrow size distribution. However, the underlying mechanism of
precipitation polymerization has not been fully understood. In particular,
the crucial early stages of microgel formation have been poorly investigated
so far. In this contribution, we have used small-angle neutron scattering
in conjunction with a stopped-flow device to monitor the particle
growth during precipitation polymerization in situ. The average particle
volume growth is found to follow pseudo-first order kinetics, indicating
that the polymerization rate is determined by the availability of
the unreacted monomer, as the initiator concentration does not change
considerably during the reaction. This is confirmed by calorimetric
investigation of the polymerization process. Peroxide initiator-induced
self-crosslinking of
N
-isopropylacrylamide and the
use of the bifunctional crosslinker
N
,
N
′-methylenebisacrylamide are shown to decrease the particle
number density in the batch. The results of the in situ small-angle
neutron scattering measurements indicate that the particles form at
an early stage in the reaction and their number density remains approximately
the same thereafter. The overall reaction rate is found to be sensitive
to monomer and initiator concentration in accordance with a radical
solution polymerization mechanism, supporting the results from our
earlier studies.
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