Modelling and Simulation of Multi-vessel Batch Distillation Column

Market demand of specialty chemicals, biochemical and pharmaceuticals are increasing. Batch distillation is considered as the most suitable distillation operation to separate all those chemicals due to its flexibility, operability and lower capital cost. Multi-vessel batch distillation is an improve...

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Main Authors:	Nurul Hazwani, Sabri, Anwaruddin, Hisyam, Badhrulhisham, Abdul Aziz
Format:	Article
Language:	English
Published:	AIDIC Servizi 2017
Subjects:	TP Chemical technology
Online Access:	http://umpir.ump.edu.my/id/eprint/17902/ http://umpir.ump.edu.my/id/eprint/17902/ http://umpir.ump.edu.my/id/eprint/17902/1/fkksa-2017-hazwani-Modelling%20and%20simulation%20of%20multi.pdf

id	ump-17902
recordtype	eprints
spelling	ump-179022018-04-18T00:53:24Z http://umpir.ump.edu.my/id/eprint/17902/ Modelling and Simulation of Multi-vessel Batch Distillation Column Nurul Hazwani, Sabri Anwaruddin, Hisyam Badhrulhisham, Abdul Aziz TP Chemical technology Market demand of specialty chemicals, biochemical and pharmaceuticals are increasing. Batch distillation is considered as the most suitable distillation operation to separate all those chemicals due to its flexibility, operability and lower capital cost. Multi-vessel batch distillation is an improvement of less energy efficient batch distillation. This paper focuses on modelling and simulation of multi vessel batch distillation column under total reflux operation for separating a ternary mixture. Total reflux operation leads to production of high purity product. In industry, the modelling and simulation play a very important role. It can help with the description of the system and the choice of the optimal control strategy. The main objective of this paper is to determine the mathematical model of multi-vessel batch distillation which usually precedes the design of the controller. Mathematical model is firstly developed based on the first principles and ordinary differential equations (ODE). MATLAB Simulink is employed to perform the simulation. The vessel holdup is set based on product purity. The model is expected to produce stable response with the changing inputs variables and produce high purity product. The control strategy is determined. AIDIC Servizi 2017 Article PeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/17902/1/fkksa-2017-hazwani-Modelling%20and%20simulation%20of%20multi.pdf Nurul Hazwani, Sabri and Anwaruddin, Hisyam and Badhrulhisham, Abdul Aziz (2017) Modelling and Simulation of Multi-vessel Batch Distillation Column. Chemical Engineering Transactions, 56. pp. 1136-1140. ISSN 22283-9216 http://www.aidic.it/cet/17/56/190.pdf
repository_type	Digital Repository
institution_category	Local University
institution	Universiti Malaysia Pahang
building	UMP Institutional Repository
collection	Online Access
language	English
topic	TP Chemical technology
spellingShingle	TP Chemical technology Nurul Hazwani, Sabri Anwaruddin, Hisyam Badhrulhisham, Abdul Aziz Modelling and Simulation of Multi-vessel Batch Distillation Column
description	Market demand of specialty chemicals, biochemical and pharmaceuticals are increasing. Batch distillation is considered as the most suitable distillation operation to separate all those chemicals due to its flexibility, operability and lower capital cost. Multi-vessel batch distillation is an improvement of less energy efficient batch distillation. This paper focuses on modelling and simulation of multi vessel batch distillation column under total reflux operation for separating a ternary mixture. Total reflux operation leads to production of high purity product. In industry, the modelling and simulation play a very important role. It can help with the description of the system and the choice of the optimal control strategy. The main objective of this paper is to determine the mathematical model of multi-vessel batch distillation which usually precedes the design of the controller. Mathematical model is firstly developed based on the first principles and ordinary differential equations (ODE). MATLAB Simulink is employed to perform the simulation. The vessel holdup is set based on product purity. The model is expected to produce stable response with the changing inputs variables and produce high purity product. The control strategy is determined.
format	Article
author	Nurul Hazwani, Sabri Anwaruddin, Hisyam Badhrulhisham, Abdul Aziz
author_facet	Nurul Hazwani, Sabri Anwaruddin, Hisyam Badhrulhisham, Abdul Aziz
author_sort	Nurul Hazwani, Sabri
title	Modelling and Simulation of Multi-vessel Batch Distillation Column
title_short	Modelling and Simulation of Multi-vessel Batch Distillation Column
title_full	Modelling and Simulation of Multi-vessel Batch Distillation Column
title_fullStr	Modelling and Simulation of Multi-vessel Batch Distillation Column
title_full_unstemmed	Modelling and Simulation of Multi-vessel Batch Distillation Column
title_sort	modelling and simulation of multi-vessel batch distillation column
publisher	AIDIC Servizi
publishDate	2017
url	http://umpir.ump.edu.my/id/eprint/17902/ http://umpir.ump.edu.my/id/eprint/17902/ http://umpir.ump.edu.my/id/eprint/17902/1/fkksa-2017-hazwani-Modelling%20and%20simulation%20of%20multi.pdf
first_indexed	2023-09-18T22:25:01Z
last_indexed	2023-09-18T22:25:01Z
_version_	1777415908213391360

Modelling and Simulation of Multi-vessel Batch Distillation Column

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