This paper is concerned with the computational aspects of countercurrent multicomponent separation processes using a nonequilibrium stage model. The developed program solves the component material and energy balance relations for each phase together with mass and energy transfer rate equations and equilibrium equations for the interface. The program is formulated in such a way as to make the describing equations and the method of solving them independent of the methods used to predict the vapor and liquid multicomponent mass transfer coefficients and heat transfer coefficients as well as physical properties like density, viscosity, binary diffusion coefficients. component specific heats and thermal conductivity, and the thermodynamic proper...
A nonequilibrium (NEQ) model for a complete three-phase distillation in tray columns is described. T...
A nonequilibrium (NEQ) model for a complete three-phase distillation in tray columns is described. T...
This paper presents a model for the calculation of Murphree point efficiencies in distillation on no...
Most models available for simulation of multicomponent separation processes are based on the idealiz...
A generic nonequilibrium cell model for multicomponent separation processes, including liquid-phase ...
This report gives a summary of the research accomplished under this project which included: Collocat...
A generic nonequilibrium cell model for multicomponent separation processes, including liquid-phase ...
This work has two major objectives: (1) To develop reliable, stable, easily-programmable and fast c...
This work has two major objectives: (1) To develop reliable, stable, easily-programmable and fast c...
In this chapter, an algorithm for the solution of the mathematical model featuring steady‐state mult...
The concept of distillation separation feasibility is investigated using reduced-order models. Thre...
The material and energy balance equations for a batch distillation column were derived and a compute...
The large dimensionality of the system of algebraic (and differential) equations of the models for p...
This paper presents modeling and simulation studies of distillation column. This study is to stimula...
Dynamic simulation programs were created in the Python programming language, to describe a laborator...
A nonequilibrium (NEQ) model for a complete three-phase distillation in tray columns is described. T...
A nonequilibrium (NEQ) model for a complete three-phase distillation in tray columns is described. T...
This paper presents a model for the calculation of Murphree point efficiencies in distillation on no...
Most models available for simulation of multicomponent separation processes are based on the idealiz...
A generic nonequilibrium cell model for multicomponent separation processes, including liquid-phase ...
This report gives a summary of the research accomplished under this project which included: Collocat...
A generic nonequilibrium cell model for multicomponent separation processes, including liquid-phase ...
This work has two major objectives: (1) To develop reliable, stable, easily-programmable and fast c...
This work has two major objectives: (1) To develop reliable, stable, easily-programmable and fast c...
In this chapter, an algorithm for the solution of the mathematical model featuring steady‐state mult...
The concept of distillation separation feasibility is investigated using reduced-order models. Thre...
The material and energy balance equations for a batch distillation column were derived and a compute...
The large dimensionality of the system of algebraic (and differential) equations of the models for p...
This paper presents modeling and simulation studies of distillation column. This study is to stimula...
Dynamic simulation programs were created in the Python programming language, to describe a laborator...
A nonequilibrium (NEQ) model for a complete three-phase distillation in tray columns is described. T...
A nonequilibrium (NEQ) model for a complete three-phase distillation in tray columns is described. T...
This paper presents a model for the calculation of Murphree point efficiencies in distillation on no...