High-pressure technology for polyethylene production has been widely used by industries around the world. The high-pressure autoclave reactor model developed in this work is based on a non-isothermal dynamic model, where PID control equations are used to maintain the operation at the unstable steady state. Kinetic mechanisms to describe the polymerization rate and molecular weight averages are presented. The model is capable of computing temperature, concentration gradients and polymer characteristics. The model was validated using industrial data, presenting good representation of the behavior of the autoclave reactor. © 2006 Elsevier B.V. All rights reserved.21C639644Chan, W.M., Gloor, P.E., Hamielec, A.E., (1993) AIChE.J., 39, pp. 111-12...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
A new steady-state model incorporating interactions between separate bubble and emulsion phases insi...
Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)High-pressure technology for pol...
: A polimerização a alta pressão em reator autoclave é uma das tecnologias empregadas na produção de...
We have incorporated mass balances of monomer, radical and polymer species to a previously developed...
A gPROMS implementation of a comprehensive steady-state model of the high-pressure polymerization of...
A thorough model of the high pressure polymerization of ethylene in tubular reactors previously deve...
A rigorous dynamic model of the high-pressure polymerization of ethylene in tubular reactors is pres...
Various applications of modeling in the field of polymerization reaction engineering are demonstrate...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
A dynamic model of a slurry polymerization stirred tank reactor for the production of high-density p...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
A new steady-state model incorporating interactions between separate bubble and emulsion phases insi...
Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)High-pressure technology for pol...
: A polimerização a alta pressão em reator autoclave é uma das tecnologias empregadas na produção de...
We have incorporated mass balances of monomer, radical and polymer species to a previously developed...
A gPROMS implementation of a comprehensive steady-state model of the high-pressure polymerization of...
A thorough model of the high pressure polymerization of ethylene in tubular reactors previously deve...
A rigorous dynamic model of the high-pressure polymerization of ethylene in tubular reactors is pres...
Various applications of modeling in the field of polymerization reaction engineering are demonstrate...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
A dynamic model of a slurry polymerization stirred tank reactor for the production of high-density p...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
Different approaches to modeling the gas phase polymerization of ethylene that have been considered ...
A new steady-state model incorporating interactions between separate bubble and emulsion phases insi...