A methodology for parameter estimation in chromatographic models is suggested in this paper, which is based on breakthrough curves from a given column set-up. Physical parameters are found in two subsequent experiments, one for the mobile phase behaviour and one for the stationary phase behaviour. The estimations are based on flow rate changes and multiple responses. Adsorption parameters are found also in two subsequent experiments, one for isotherm parameters and one for kinetics parameters. These estimations are based on concentration changes. The conclusion is that it is possible to estimate the parameters in a general rate model using nonlinear least square estimation and numerical simulation of the model. Copyright (C) 2001 IFAC
The shape of breakthrough curves and elution profiles depends strongly on the course of the specific...
The shape of breakthrough curves and elution profiles depends strongly on the course of the specific...
A method for estimation of unknown adsorption parameters in a detailed chromatography model includin...
Artículo de publicación ISIThe most used mathematical models with a phenomenological basis for simul...
Artículo de publicación ISIThe most used mathematical models with a phenomenological basis for simul...
A methodology for estimation of the unknown physical parameters in a detailed model for chromatograp...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
A methodology for estimation of the dependency on flow rate and bead size of the axial dispersion co...
The shape of breakthrough curves and elution profiles depends strongly on the course of the specific...
The industrial chromatographic purification of biotechnological products, such as milk powder or ins...
The industrial chromatographic purification of biotechnological products, such as milk powder or ins...
The shape of breakthrough curves and elution profiles depends strongly on the course of the specific...
The shape of breakthrough curves and elution profiles depends strongly on the course of the specific...
A method for estimation of unknown adsorption parameters in a detailed chromatography model includin...
Artículo de publicación ISIThe most used mathematical models with a phenomenological basis for simul...
Artículo de publicación ISIThe most used mathematical models with a phenomenological basis for simul...
A methodology for estimation of the unknown physical parameters in a detailed model for chromatograp...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
In this work a new mathematical model, based on non-equilibrium conditions, describing the dynamic a...
A methodology for estimation of the dependency on flow rate and bead size of the axial dispersion co...
The shape of breakthrough curves and elution profiles depends strongly on the course of the specific...
The industrial chromatographic purification of biotechnological products, such as milk powder or ins...
The industrial chromatographic purification of biotechnological products, such as milk powder or ins...
The shape of breakthrough curves and elution profiles depends strongly on the course of the specific...
The shape of breakthrough curves and elution profiles depends strongly on the course of the specific...
A method for estimation of unknown adsorption parameters in a detailed chromatography model includin...