2009
DOI: 10.1021/ma9018685
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Theoretical Analysis of the Copolymer Composition Equation in Chain Shuttling Copolymerization

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Cited by 24 publications
(36 citation statements)
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“…[12,13] Because this approach cannot generate detailed microstructural distributions, Monte Carlo (MC) models were later developed for OBCs made in CSTRs operated at steadystate. [14][15][16] Subsequently, Mohammadi et al developed Chain-shuttling polymerization with dual catalysts has introduced a new class of polyolefins called olefin block copolymers (OBCs). A dynamic Monte Carlo model to describe the kinetics of chain-shuttling copolymerization in a semi-batch reactor is developed, and used it to study how the microstructure of OBCs with different numbers of blocks per chain evolves during polymerization.…”
mentioning
confidence: 99%
“…[12,13] Because this approach cannot generate detailed microstructural distributions, Monte Carlo (MC) models were later developed for OBCs made in CSTRs operated at steadystate. [14][15][16] Subsequently, Mohammadi et al developed Chain-shuttling polymerization with dual catalysts has introduced a new class of polyolefins called olefin block copolymers (OBCs). A dynamic Monte Carlo model to describe the kinetics of chain-shuttling copolymerization in a semi-batch reactor is developed, and used it to study how the microstructure of OBCs with different numbers of blocks per chain evolves during polymerization.…”
mentioning
confidence: 99%
“…The copolymer composition directly reflects the chemical structure of polymers; thus, the composition equation is used to evaluate instantaneous composition of the bipolymers in light of the following formula [17,18]. F1=r1f12+f1f22a F2=1(r11)f22+(12r1)f2+r1(r12+r2)f22+2(1r1)f2+r1 where F 1 and F 2 are the molar ratios of AM and cationic monomer to the total copolymer units, respectively; f 1 and f 2 are the molar ratios of AM and cationic monomer to all material monomers before polymerization, respectively; and r 1 and r 2 are the monomer reactivity ratios obtained from Section 2.3.…”
Section: Methodsmentioning
confidence: 99%
“…Modeling studies reported so far were devoted to the analysis of copolymer composition, molecular weight distribution, length of the blocks, distribution of the number of blocks per chain and to finer microstructure analysis and its evolution during the polymerization . It has notably been shown that the Mayo − Lewis equation may no longer be able to describe the composition of the copolymers formed instantaneously by each catalyst in CSP systems operating in a continuous stirred tank reactor (CSTR) . This may arise when the chain transfer rate is substantially higher than the propagation rate, and may not be the case when a single catalyst is used in the presence of a chain transfer agent.…”
Section: Theoretical Modeling Of Cspmentioning
confidence: 99%
“…Steric hindrance as well as chain growth on the magnesium atom have been advanced to explain these effects. It should finally be noted that (i) several studies dealing with CCTcoP did not report significant changes in the copolymerization reactivity ratio and (ii) theoretical modeling in a CSTR does not predict such changes in the case of single catalyst/chain transfer agent mediated statistical copolymerization (CCTcoP).…”
Section: Unexpected Reactivities Observed In Coordinative Chain Transmentioning
confidence: 99%