“…In aqueous solution, k p varies with monomer concentration and thus also during the course of a polymerization to high conversion, where the ratio of monomer-to-water concentration changes. Consistent with what has been found for methacrylic acid, [12] recent investigations into aqueoussolution polymerization of 1-vinylpyrrolidin-2-one (VP) in the presence of different amounts of premixed poly-(1-vinylpyrrolidin-2-one) (poly(VP)), which mimics monomer conversion, revealed that it is the ratio of monomeric VP-to-water concentration which affects k p . [15] Implementing the k p data that is available for VP polymerizations at various initial monomer concentrations and up to different degrees of monomer-to-polymer conversion, k t may be derived via SP-PLP-NIR measurements on aqueous-solution VP polymerizations over an extended concentration and conversion range and up to high pressure.…”
supporting
confidence: 59%
“…It was recently shown, that k p depends on the monomer-to-water ratio, whereas the content of high-molecular-mass polymer plays no role. [12,15] The weight fraction of VP, w VP , during polymerization to high degrees of monomer conversion, X, is represented by Equation (2):…”
Section: Resultsmentioning
confidence: 99%
“…As mentioned by Beuermann et al, [12] polymer may affect k p only under conditions of very high polymer content or in case that polymer is of low molar mass and should be better referred to as oligomeric material. Combining Equation (1) and (2) with the volume of activation for propagation of VP, DV z (k p ) ¼ À11.3 cm 3 Á mol À1 , [28] yields k p for 40 8C as a function of pressure, p, initial weight fraction of VP, and monomer conversion:…”
Termination kinetics of 1‐vinylpyrrolidin‐2‐one radical polymerization in aqueous solution has been studied at 40 °C between 20 and 100 wt.‐% VP. The <kt>/kp values from laser single‐pulse experiments with microsecond time‐resolved NIR detection of monomer conversion, in conjunction with kp from literature, yield chain‐length‐averaged termination rate coefficients, <kt>. Because of better signal‐to‐noise quality, experiments were carried out at 2 000 bar, but also at 1 500, 1 000, and 500 bar, thus allowing for estimates of <kt> at ambient pressure. The dependence of <kt> on monomer conversion indicates initial control by segmental diffusion followed by translational diffusion and finally reaction diffusion control. To assist the kinetic studies, viscosities of VP–water mixtures at ambient pressure have been determined. magnified image
“…In aqueous solution, k p varies with monomer concentration and thus also during the course of a polymerization to high conversion, where the ratio of monomer-to-water concentration changes. Consistent with what has been found for methacrylic acid, [12] recent investigations into aqueoussolution polymerization of 1-vinylpyrrolidin-2-one (VP) in the presence of different amounts of premixed poly-(1-vinylpyrrolidin-2-one) (poly(VP)), which mimics monomer conversion, revealed that it is the ratio of monomeric VP-to-water concentration which affects k p . [15] Implementing the k p data that is available for VP polymerizations at various initial monomer concentrations and up to different degrees of monomer-to-polymer conversion, k t may be derived via SP-PLP-NIR measurements on aqueous-solution VP polymerizations over an extended concentration and conversion range and up to high pressure.…”
supporting
confidence: 59%
“…It was recently shown, that k p depends on the monomer-to-water ratio, whereas the content of high-molecular-mass polymer plays no role. [12,15] The weight fraction of VP, w VP , during polymerization to high degrees of monomer conversion, X, is represented by Equation (2):…”
Section: Resultsmentioning
confidence: 99%
“…As mentioned by Beuermann et al, [12] polymer may affect k p only under conditions of very high polymer content or in case that polymer is of low molar mass and should be better referred to as oligomeric material. Combining Equation (1) and (2) with the volume of activation for propagation of VP, DV z (k p ) ¼ À11.3 cm 3 Á mol À1 , [28] yields k p for 40 8C as a function of pressure, p, initial weight fraction of VP, and monomer conversion:…”
Termination kinetics of 1‐vinylpyrrolidin‐2‐one radical polymerization in aqueous solution has been studied at 40 °C between 20 and 100 wt.‐% VP. The <kt>/kp values from laser single‐pulse experiments with microsecond time‐resolved NIR detection of monomer conversion, in conjunction with kp from literature, yield chain‐length‐averaged termination rate coefficients, <kt>. Because of better signal‐to‐noise quality, experiments were carried out at 2 000 bar, but also at 1 500, 1 000, and 500 bar, thus allowing for estimates of <kt> at ambient pressure. The dependence of <kt> on monomer conversion indicates initial control by segmental diffusion followed by translational diffusion and finally reaction diffusion control. To assist the kinetic studies, viscosities of VP–water mixtures at ambient pressure have been determined. magnified image
“…This insensitivity of (bulk polymerization) k p toward the degree of monomer conversion must not hold in solution polymerizations, as has been demonstrated for MAA polymerizations in aqueous solution, [11] where k p was observed to increase toward higher degrees of monomer conversion. This effect may also be adequately understood on the basis of the genuine kinetic argument that it is the friction experienced by the TS structure which controls A(k p ).…”
Summary: Pulsed laser techniques have enormously improved the quality by which rate coefficients of radical polymerization may be determined. The specific and most important feature of the various types of pulsed laser techniques consists in the almost instantaneous production of a significant radical concentration and in the ease by which radical concentration may be controlled by applying further laser pulses at pre-selected delay times. The pulsed laser polymerization -size exclusion chromatography (PLP-SEC) experiment is extremely valuable for the determination of reliable propagation rate coefficients, k p . The present article briefly reviews recent results from PLP-SEC studies directed toward the solvent dependence of k p in aqueous systems, into k p in copolymerization reactions, and into measurements of propagation rate coefficients in systems containing two types of radicals, as is the case with acrylates, where secondary chain-end radicals may undergo 1,5-H shift reactions (backbiting steps) to produce tertiary midchain radicals. By a propagation step, the tertiary radicals are transformed back to secondary ones.
“…To study the influence of monomer conversion on k p , PLP-SEC was conducted on reaction mixtures containing different amounts of polymer from the preceding polymerization. [56,58] The experiments were carried out for methacrylic acid and N-vinyl pyrrolidone. The concentrations were chosen such that the reaction mixture mimics a polymerizing system initially containing 20 wt.-% of monomer.…”
Section: Polymerizations In Aqueous Phasementioning
The influence of the reaction medium (organic solvents, water, ionic liquids, supercritical CO(2) ) on the propagation rate in radical polymerizations has very different causes, e.g., hindered rotational modes, hydrogen bonding or electron pair donor/acceptor interactions. Depending on the origin of the solvent influence propagation rate coefficients, k(p) , may be enhanced by up to an order of magnitude associated with changes in the pre-exponential or the activation energy of k(p) . In contrast, non-specific interactions, size and steric effects lead to rather small changes in the vicinity of the radical chain end and are reflected by modest variations in k(p) .
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