Volume no :10, Issue no: 2, November (2013)

A NEW APPROACH FOR THE COLUMN APPARATUSES MODELLING IN CHEMICAL ENGINEERING

Author's: CHR. BOYADJIEV
Pages: [131] - [150]
Received Date: December 12, 2012; Revised January 26, 2013
Submitted by:

Abstract

The column apparatuses are main devices for solution of technological and ecological problems in chemical engineering. A new approach of the column apparatuses modelling on the base of two steps models - diffusion type of model (for qualitative analysis) and average concentration model (for quantitative analysis) is presented.

The diffusion type of models are obtained on the base of the physical approximations of the mechanics of continua, where the mathematical point is equivalent to a small (elementary) physical volume, which is sufficiently small with respect to the apparatus volume, but at the same time sufficiently large with respect to the intermolecular volumes of the medium. As a result, the mathematical model is mass balance in this elementary volume in convection-diffusion equation form.

The diffusion type of models describe chemical and mass transfer processes in column apparatuses in the cases of one, two or three phases systems, where the solid phase is reagent, catalytic or packed bad. A qualitative analysis of these models is presented, using generalized (dimensionless) variables, where the characteristic (inherent) scales are the maximal or average values of the variables. As a result is possible to be identified the main physical effect, the small physical effect and the very small (negligible) physical effect, which must be neglected because it is not possible to be measured experimentally. The diffusion type of models are the base for the creation of the average concentration models.

The using of the diffusion type of models for quantitative analysis of the processes in column apparatuses is not possible because the velocity function in the convection-diffusion equation is unknown. The problem can be avoided if the average values of the velocity and concentration over the cross-sectional area of the column are used, i.e., the medium elementary volume (in the physical approximations of the mechanics of continua) will be equivalent to a small cylinder with radius equal to the column radius and a height, which is sufficiently small with respect to the column height and at the same time sufficiently large with respect to the intermolecular distances in the medium.

The average concentration models permit to analyze the effect of the radial nonuniformities of the velocity and the concentration on the process efficiency in the column and to solve the scale-up problem.

The new approach of the column apparatuses modelling is used for modelling of physical and chemical absorption, chemical adsorption, homogeneous and heterogeneous (catalytic) chemical reactions, airlift reactors for chemical and photochemical reactions.

Keywords

mathematical modelling, mechanics of continua, column apparatus, diffusion type of model, average concentration of model.