MODELING AND CONTROL OF MINI DISTILLATION COLUMN USING SLIDING MODE CONTROLLER

This thesis presents the model and control design of distillation process as a common component separation process in chemical operations. Mini distillation column for laboratory scale is used to separate ethanol and water components. Distillation process is carried out by charged the liquid compone...

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Main Author: MAULIDDA (NIM : 23215069), RENNY
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/23891
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:23891
spelling id-itb.:238912017-09-28T16:05:21ZMODELING AND CONTROL OF MINI DISTILLATION COLUMN USING SLIDING MODE CONTROLLER MAULIDDA (NIM : 23215069), RENNY Indonesia Theses INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/23891 This thesis presents the model and control design of distillation process as a common component separation process in chemical operations. Mini distillation column for laboratory scale is used to separate ethanol and water components. Distillation process is carried out by charged the liquid components into the heater pot which is called batch process. Batch distillation column modeling is obtained by deriving mathematically the chemical and physical processes during the distillation process. Equations of modeling are expressed based on equilibrium component mass, vapor-liquid equilibrium (VLE) and other physical characteristics. From the derivation of mathematical equations, nonlinear system model is obtained. The model is simulated by MATLAB software and validated with data on real plant experiment. <br /> <br /> In this study, in order to design the sliding mode controller, a model of the identification system is built because the nonlinear inverse of the mathematical equations is undefined in the sliding mode controller. The experimental data in system identification is the water concentration data that represents the linear system. The identification result shows that the distillation column model has been appropriated with the experimental data response with 91.78% of fit percentage match. <br /> <br /> From the linear model, the simulation of sliding mode controller method is used by linear continuous feedback approach to produce the pure distillate of ethanol concentration by desired concentration, which is the output of the distillation system. The design of an observer for a closed loop system is used to estimate an unmeasured state variable. The results of the sliding mode control simulation show that the system is stable in closed loop system and has been able to follow the given reference. text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description This thesis presents the model and control design of distillation process as a common component separation process in chemical operations. Mini distillation column for laboratory scale is used to separate ethanol and water components. Distillation process is carried out by charged the liquid components into the heater pot which is called batch process. Batch distillation column modeling is obtained by deriving mathematically the chemical and physical processes during the distillation process. Equations of modeling are expressed based on equilibrium component mass, vapor-liquid equilibrium (VLE) and other physical characteristics. From the derivation of mathematical equations, nonlinear system model is obtained. The model is simulated by MATLAB software and validated with data on real plant experiment. <br /> <br /> In this study, in order to design the sliding mode controller, a model of the identification system is built because the nonlinear inverse of the mathematical equations is undefined in the sliding mode controller. The experimental data in system identification is the water concentration data that represents the linear system. The identification result shows that the distillation column model has been appropriated with the experimental data response with 91.78% of fit percentage match. <br /> <br /> From the linear model, the simulation of sliding mode controller method is used by linear continuous feedback approach to produce the pure distillate of ethanol concentration by desired concentration, which is the output of the distillation system. The design of an observer for a closed loop system is used to estimate an unmeasured state variable. The results of the sliding mode control simulation show that the system is stable in closed loop system and has been able to follow the given reference.
format Theses
author MAULIDDA (NIM : 23215069), RENNY
spellingShingle MAULIDDA (NIM : 23215069), RENNY
MODELING AND CONTROL OF MINI DISTILLATION COLUMN USING SLIDING MODE CONTROLLER
author_facet MAULIDDA (NIM : 23215069), RENNY
author_sort MAULIDDA (NIM : 23215069), RENNY
title MODELING AND CONTROL OF MINI DISTILLATION COLUMN USING SLIDING MODE CONTROLLER
title_short MODELING AND CONTROL OF MINI DISTILLATION COLUMN USING SLIDING MODE CONTROLLER
title_full MODELING AND CONTROL OF MINI DISTILLATION COLUMN USING SLIDING MODE CONTROLLER
title_fullStr MODELING AND CONTROL OF MINI DISTILLATION COLUMN USING SLIDING MODE CONTROLLER
title_full_unstemmed MODELING AND CONTROL OF MINI DISTILLATION COLUMN USING SLIDING MODE CONTROLLER
title_sort modeling and control of mini distillation column using sliding mode controller
url https://digilib.itb.ac.id/gdl/view/23891
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