A mathematical model was developed to simulate the operation of a narrow-cut fractionating column. The model can calculate boiling point and dew point on the feed plate, the number of liquid and vapour moles, the enthalpy of feed and the final product distribution at the top and bottom of the column. The 6-method of convergence for predicting the product composition in bottom product and distillate corresponding to different operating conditions was used. The model was tested using different top pressures (5-30 psig), different feed temperatures (77-107T) and different reflux ratios (1:1 to 1:3). The most effective variable was found to be top pressure. Decreasing the number of plates improved the convergence. Also increasing the number of ...
AbstractBatch distillation is a very efficient unit operation which allows the fractionation of a mu...
The article is devoted to the study of methods for modeling the operation of rectification columns u...
AM-A generalized model for the dynamic simulation of distillation columns is presented. The model al...
In an effort to simulate the separation of multicomponent mixtures on the plates of distillation col...
Vita.The work which follows contributes several methods for solving problems involving fractionating...
This work aims to study the quality of three products of a fractionation column considering differen...
This report gives a summary of the research accomplished under this project which included: Collocat...
The purpose of this investigation was to study. the effect of slot velocity, liquid height, plate sp...
A study has been made using computer simulation of a fractionating column with simultaneous distilla...
A new methodology for the optimisation of feed conditions as well as the calculation of minimum refl...
ii In this thesis we present a collocation method originally developed for minimum reflux calculatio...
Traditionally, the production of three high purity products from a three component mixture requires ...
A novel method is presented in this paper to quantitatively define the heat removal of the main frac...
In this analysis, based on the bubble point method, a physical model wasestablished clarifying the i...
The paper considers the effect of feed plate location on the interactions in a seven plate binary di...
AbstractBatch distillation is a very efficient unit operation which allows the fractionation of a mu...
The article is devoted to the study of methods for modeling the operation of rectification columns u...
AM-A generalized model for the dynamic simulation of distillation columns is presented. The model al...
In an effort to simulate the separation of multicomponent mixtures on the plates of distillation col...
Vita.The work which follows contributes several methods for solving problems involving fractionating...
This work aims to study the quality of three products of a fractionation column considering differen...
This report gives a summary of the research accomplished under this project which included: Collocat...
The purpose of this investigation was to study. the effect of slot velocity, liquid height, plate sp...
A study has been made using computer simulation of a fractionating column with simultaneous distilla...
A new methodology for the optimisation of feed conditions as well as the calculation of minimum refl...
ii In this thesis we present a collocation method originally developed for minimum reflux calculatio...
Traditionally, the production of three high purity products from a three component mixture requires ...
A novel method is presented in this paper to quantitatively define the heat removal of the main frac...
In this analysis, based on the bubble point method, a physical model wasestablished clarifying the i...
The paper considers the effect of feed plate location on the interactions in a seven plate binary di...
AbstractBatch distillation is a very efficient unit operation which allows the fractionation of a mu...
The article is devoted to the study of methods for modeling the operation of rectification columns u...
AM-A generalized model for the dynamic simulation of distillation columns is presented. The model al...