Abstract:In this paper, random copolymer of styrene (St) and maleic anhydride (MAH) were prepared by stabilizer-free dispersion polymerization, with dicumyl peroxide (DCP) as initiator and ethyl butyrate as solvent at 120 • C. The microsphere morphology and sequential structure of the copolymers were characterized by SEM and 13 C-NMR, respectively. When the molar feed ratio of MAH to St (MAH/St) was 20/80, the overall MAH content in the copolymer was about 26% (molar) from the 13 C-NMR spectrum, and the three St-centre… Show more
“…Moreover, the high monomer concentration and particle yield provide this method with intensive potential for broad industrial applications. Therefore, many functional polymer particles with a well-defined morphology have been prepared via 2SP since the first report of 2SP of MAH and vinyl acetate by Xing. ,,− So far, the monomers for 2SP are mainly composed of electron-donating monomers (olefinic compounds) and electron-accepting monomers (MAH and its derivatives). Though AM is also an electron-accepting monomer, the 2SP of AM is not that simple due to the poor solubility of PAMs in common solvents.…”
In this paper, we report for the first time the selfstabilized precipitation polymerization of styrene (St), maleic anhydride (MAH), and acrylamide (AM) in isoamyl acetate as the reaction medium. The effects of various reaction parameters, including the reaction medium, monomer concentration, reaction time, and monomer feed ratio, on the morphology and chemical composition of the resultant poly(St/MAH/AM) terpolymer particles were investigated systematically. The experimental results demonstrated that uniform poly(St/MAH/AM) terpolymer particles with the diameter in the range of 50 to 2000 nm were facilely obtained over a wide range of monomer feed ratios of St/MAH/AM (from 40:40:20 to 10:10:80). Furthermore, the chemical composition of the terpolymer particles was largely dependent on the initial monomer feed ratio, which remained almost constant irrelevant of reaction time when the molar ratio of [St]/[MAH] was 1:1. Therefore, the poly(St/MAH/AM) terpolymer particles with a well-defined morphology, uniform size, and controlled chemical composition can be efficiently synthesized via this method, and the anhydride and amide functional groups provide poly(St/MAH/AM) particles with intensive potential for various applications.
“…Moreover, the high monomer concentration and particle yield provide this method with intensive potential for broad industrial applications. Therefore, many functional polymer particles with a well-defined morphology have been prepared via 2SP since the first report of 2SP of MAH and vinyl acetate by Xing. ,,− So far, the monomers for 2SP are mainly composed of electron-donating monomers (olefinic compounds) and electron-accepting monomers (MAH and its derivatives). Though AM is also an electron-accepting monomer, the 2SP of AM is not that simple due to the poor solubility of PAMs in common solvents.…”
In this paper, we report for the first time the selfstabilized precipitation polymerization of styrene (St), maleic anhydride (MAH), and acrylamide (AM) in isoamyl acetate as the reaction medium. The effects of various reaction parameters, including the reaction medium, monomer concentration, reaction time, and monomer feed ratio, on the morphology and chemical composition of the resultant poly(St/MAH/AM) terpolymer particles were investigated systematically. The experimental results demonstrated that uniform poly(St/MAH/AM) terpolymer particles with the diameter in the range of 50 to 2000 nm were facilely obtained over a wide range of monomer feed ratios of St/MAH/AM (from 40:40:20 to 10:10:80). Furthermore, the chemical composition of the terpolymer particles was largely dependent on the initial monomer feed ratio, which remained almost constant irrelevant of reaction time when the molar ratio of [St]/[MAH] was 1:1. Therefore, the poly(St/MAH/AM) terpolymer particles with a well-defined morphology, uniform size, and controlled chemical composition can be efficiently synthesized via this method, and the anhydride and amide functional groups provide poly(St/MAH/AM) particles with intensive potential for various applications.
“…Another relevant fact regarding the copolymer is that the copolymerization between ST/MAH is widely known as an alternating copolymerization, − which points to the solvent as the most significant factor for the system stability and final particle diameter. Some authors suggest that particle stabilization in the stabilizer-free case may result from the affinity between the polymer particles and the ester groups in the reaction medium. − Also, the soluble polymer formed in situ may act as the stabilizer, preventing complete coagulation of the system. − Therefore, a particle formation model would help in understanding the nucleation in stabilizer-free polymerization systems, especially for the IBA and IPA case.…”
Section: Resultsmentioning
confidence: 99%
“…Dispersion polymerization can also be carried out in the absence of a stabilizing agent and, in this case, it is called stabilizer-free dispersion polymerization. − The literature shows that only some organic solvents lead to the formation of uniform, monodisperse particles, for instance, alkyls esters. Moreover, all of the stabilizer-free systems that allowed particle formation were copolymerization reactions between maleic anhydride (MAH) and another monomer, such as styrene (ST) or vinyl acetate (VA). − …”
Section: Introductionmentioning
confidence: 99%
“…Some authors suggest that particle stabilization may result from the affinity between the polymer particles and the ester groups in the reaction medium. In addition, the polymer formed in situ may act as the particle stabilizer, preventing complete system coagulation. − …”
This work proposes a new model for
particle nucleation, in addition
to particle growth, in the process of stabilizer-free dispersion copolymerization
of styrene and maleic anhydride in organic solvents. This paper provides
the first contribution to the modeling and simulation of the nucleation
step in this process. The model considers that (1) polymerization
takes place in both the continuous phase and the polymer particles;
(2) radicals in the continuous phase that exceed the size J
crit precipitate and form aggregates; (3) the
coagulation between aggregates forms new particles; (4) the radicals
in the continuous phase can also enter into the polymer particles,
reducing the nucleation rate; and (5) the termination step inside
the particles is diffusion-controlled. The model is able to correctly
predict the time evolution of the monomer conversion, particle number,
and particle size and was successfully validated against data obtained
experimentally and from the literature. Different from the existing
models, the proposed model does not require previous information regarding
the particle size or number to initialize the model. The radical entry
parameter and the radical solubility are important parameters that
affect the nucleation step.
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