View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by CONICET Digital Latin American Applied Research 41: 389-401(2011) MOLECULAR WEIGHT DISTRIBUTIONS IN IDEAL POLYMERIZATION REACTORS. AN INTRODUCTORY REVIEW G.R. MEIRA† and H.M. OLIVA‡ † INTEC (Univ. Nac. del Litoral and CONICET), Santa Fe (3000), Argentina.
[email protected] ‡ Escuela de Ingeniería Química, Univ. del Zulia, Maracaibo, Venezuela.
[email protected] Abstract The ultimate aim of polymerization million tons by 2015. In volume, the annual production reaction engineering is the production of polymers of polymers exceeds that of the 2 most important met- with tailor-made properties. An introductory review als: iron and aluminum. The raw materials for the pro- into this field is presented, with emphasis on the ef- duction of around 95% of all synthetic polymers are fects on the molar mass distribution (MMD), of the non-renewable sources (fossil oil, gas, and coal). sought combination of polymerization mechanism, Polymerization Reaction Engineering deals with reactor type, and reactor control. Three ideal poly- problems involving the measurement, mathematical merization mechanisms are analyzed: free-radical, modeling, optimization, and control of industrial poly- “living” anionic, and step-growth. “Living” anionic merization processes. It aims at improving both the and step-growth polymerizations are similar in that productivity of the polymerization process and the qual- their growing chains remain reactive while inside the ity of the produced polymer. Some general references reactor; and for these systems the narrowest MMDs on this area are: Ray (1972), Reichert and Moritz are produced in reactors with narrow residence time (1989), Hamielec and Tobita (1992), Kiparissides distributions (RDT); i.e.: batch or continuous tubu- (1996), Ray et al.