EXPRESSION SYSTEMS FLUID-SOLID NO CATALYTIC, CONTROLLED BY BROADCAST PARTICLE INTERNAL FIXED SIZE. SECOND PART

  • René Viera Bertrán Facultad de Ingeniería Química, Universidad de Oriente
  • Dania del Toro Álvarez Facultad de Ingeniería Química, Universidad de Oriente
  • Antonio Pons Hernández Facultad de Ingeniería Química, Universidad de Oriente
Keywords: controlling step, internal diffusion, fluid-solid noncatalytic

Abstract

In the first part of this paper, a black box model that provided an explicit relationship between the fraction of unconverted solid reactant I and the relationship Y = t /τ.You had a set of possible applications, for systems with plug flow for the solid phase. In this second part of the work, we deduce the expressions for more complex situations, such as perfect mixing reactor to the solid phase, which are discussed in the situations described below: a single reactor mean residence time: tp; particles of one size; mixture of particles of different sizes; for two reactors with residence times equal means (tp); for three reactors with residence times equal means (tp); for four reactors with residence times equal means (tp); for five reactor residence times equal means (tp) The procedure used in deductions, can be used in other situations of interest without much difficulty. The expressions presented in addition to its ease of use, have the advantage of facilitating the manufacture of programmable algorithms.
Published
2016-03-29
How to Cite
Viera Bertrán, R., del Toro Álvarez, D., & Pons Hernández, A. (2016). EXPRESSION SYSTEMS FLUID-SOLID NO CATALYTIC, CONTROLLED BY BROADCAST PARTICLE INTERNAL FIXED SIZE. SECOND PART. Chemical Technology, 30(3), 20-30. https://doi.org/10.1590/2224-6185.2010.3.%x
Section
Artículos

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