INVESTIGADORES
VEGA Jorge Ruben
artículos
Título:
Continuous Emulsion Styrene-Butadiene Rubber (SBR) Process: Computer Simulation Study for Increasing Production and for Reducing Transients between Steady States
Autor/es:
MINARI, R.J.; GUGLIOTTA, L.M.; VEGA, J.R.; MEIRA, G.R.
Revista:
INDUSTRIAL & ENGINEERING CHEMICAL RESEARCH
Editorial:
American Chemical Society
Referencias:
Año: 2006 vol. 45 p. 245 - 257
ISSN:
0888-5885
Resumen:
The industrial production of two styrene-butadiene rubber (SBR) grades is optimized by means of a representative mathematical model. The emulsion process involves a train of seven continuously stirred-tank reactors. In the simulations, intermediate feeds of comonomers and chain transfer agent (CTA) are admitted. The steady-state (SS) productions can be increased by 8%, while maintaining the required final values of conversion, particle diameter, and molecular characteristics (Mh n, Mh w, and the average number of branches per molecule). For the same rubber grade, the polymer production can be changed with negligible generation of intermediate off-specs, by regulating the global calorimetric conversion. For changes of grade at a fixed polymer production, transient profiles of the intermediate CTA feeds are proposed. For changes of  production and grade, a sequential (rather than a simultaneous) transition seems preferable.-butadiene rubber (SBR) grades is optimized by means of a representative mathematical model. The emulsion process involves a train of seven continuously stirred-tank reactors. In the simulations, intermediate feeds of comonomers and chain transfer agent (CTA) are admitted. The steady-state (SS) productions can be increased by 8%, while maintaining the required final values of conversion, particle diameter, and molecular characteristics (Mh n, Mh w, and the average number of branches per molecule). For the same rubber grade, the polymer production can be changed with negligible generation of intermediate off-specs, by regulating the global calorimetric conversion. For changes of grade at a fixed polymer production, transient profiles of the intermediate CTA feeds are proposed. For changes of  production and grade, a sequential (rather than a simultaneous) transition seems preferable.