Texto completo: acesso restrito. p. 161-175The behavior of continuous solution ethylene/but-1-ene polymerizations through Ziegler-Natta catalysts is analyzed, based on a previously developed mathematical model. In order to do that, dynamic simulations are carried out and process responses are analyzed as functions of process operating policies and flowsheet configuration, at conditions that resemble the actual operation of industrial sites. It is shown that system responses are highly nonlinear and very sensitive to disturbances of the operating conditions and that catalyst decay is of fundamental importance for proper understanding of process behavior. Results indicate that mixing conditions inside the reactor vessels exert a significant i...
A dynamic model of a slurry polymerization stirred tank reactor for the production of high-density p...
The flow response of branched entangled resins is dominated by the branching topology of the constit...
In industrial-scale catalytic olefin copolymerization processes, catalyst and cocatalyst precontacti...
Acesso restrito: Texto completo. p. 2346-2365In this work, optimal operating policies for the ethyle...
Polyethylene (PE) is a thermoplastic polymer widely used throughout the world due to its versatile p...
Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)In this work, optimal operating p...
Texto completo: acesso restrito. p. 142-160We show that it is possible to estimate kinetic parameter...
Multizone circulating bed reactors (MZCR) have the exclusive characteristics of producing polymers o...
Mathematical models of reactors for the polymerization of methylmethacrylate (MMA) and propylene hav...
Chemical Engineering Department, King Saud University, P.O.Box 800, Riyadh 11421, Saudi ArabiaA prev...
A thorough model of the high pressure polymerization of ethylene in tubular reactors previously deve...
Modeling and optimization of olefin polymerization processes based on polymerization and process cha...
The dynamic operation of an ideal continuous-flow stirred tank slurry reactor for propylene polymeri...
This work presents the analysis of a slurry polymerization stirred tank reactor for the production o...
Modeling and optimization of olefin polymerization processes based on polymerization and process cha...
A dynamic model of a slurry polymerization stirred tank reactor for the production of high-density p...
The flow response of branched entangled resins is dominated by the branching topology of the constit...
In industrial-scale catalytic olefin copolymerization processes, catalyst and cocatalyst precontacti...
Acesso restrito: Texto completo. p. 2346-2365In this work, optimal operating policies for the ethyle...
Polyethylene (PE) is a thermoplastic polymer widely used throughout the world due to its versatile p...
Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)In this work, optimal operating p...
Texto completo: acesso restrito. p. 142-160We show that it is possible to estimate kinetic parameter...
Multizone circulating bed reactors (MZCR) have the exclusive characteristics of producing polymers o...
Mathematical models of reactors for the polymerization of methylmethacrylate (MMA) and propylene hav...
Chemical Engineering Department, King Saud University, P.O.Box 800, Riyadh 11421, Saudi ArabiaA prev...
A thorough model of the high pressure polymerization of ethylene in tubular reactors previously deve...
Modeling and optimization of olefin polymerization processes based on polymerization and process cha...
The dynamic operation of an ideal continuous-flow stirred tank slurry reactor for propylene polymeri...
This work presents the analysis of a slurry polymerization stirred tank reactor for the production o...
Modeling and optimization of olefin polymerization processes based on polymerization and process cha...
A dynamic model of a slurry polymerization stirred tank reactor for the production of high-density p...
The flow response of branched entangled resins is dominated by the branching topology of the constit...
In industrial-scale catalytic olefin copolymerization processes, catalyst and cocatalyst precontacti...