Modeling and simulation of distillation column

This paper presents modeling and simulation studies of distillation column. This study is to stimulate sieve tray distillation (rate based model) and specifically for multiple columns process by using Aspen Hysys. The economic importance of distillation separations has been a driving force for the r...

Full description

Saved in:
Bibliographic Details
Main Author: Ann, Ivy Wong Fui
Format: Undergraduates Project Papers
Language:English
Published: 2014
Subjects:
Online Access:http://umpir.ump.edu.my/id/eprint/9020/1/Modeling%20and%20simulation%20of%20distillation%20column.pdf
http://umpir.ump.edu.my/id/eprint/9020/
Tags: Add Tag
No Tags, Be the first to tag this record!
id my.ump.umpir.9020
record_format eprints
spelling my.ump.umpir.90202023-04-27T06:43:07Z http://umpir.ump.edu.my/id/eprint/9020/ Modeling and simulation of distillation column Ann, Ivy Wong Fui TP Chemical technology This paper presents modeling and simulation studies of distillation column. This study is to stimulate sieve tray distillation (rate based model) and specifically for multiple columns process by using Aspen Hysys. The economic importance of distillation separations has been a driving force for the research in synthesis procedures for more than 30 years. Distillation accounts for almost 90% of the separation systems used in chemical process industries. The best way to reduce operating costs of existing units is to improve their efficiency and operation via process optimization and control. Simulation generates one or more trajectories (possible behaviors from the high-level model), and collects statistics from these trajectories to estimate the desired performance or dependability measures. Modeling and simulation of distillation column might already be very familiar but modeling and simulation of multicomponent distillation in multiple columns still yet being commercially introduced to the industries. In this project, the well known kind of multi components (n-butane, n-pentane and benzene) is chosen as the example to run this simulation by using multiple distillation columns. By inserting the details and specifications in Aspen Hysys, multicomponents distillation process is stimulated under steady state condition. From the result gained, calculations such as compositions, temperature, mass balance and energy balance can be done step by step. The composition, k values, temperature and flowrate will be further explained in discussion. Other than that, the limitations of steady state techniques are discussed, and the need for rigorous dynamic simulation for final selection of a workable and robust strategy is illustrated 2014-01 Undergraduates Project Papers NonPeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/9020/1/Modeling%20and%20simulation%20of%20distillation%20column.pdf Ann, Ivy Wong Fui (2014) Modeling and simulation of distillation column. Faculty Of Chemical & Natural Resources Engineering, Universiti Malaysia Pahang.
institution Universiti Malaysia Pahang
building UMP Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang
content_source UMP Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Ann, Ivy Wong Fui
Modeling and simulation of distillation column
description This paper presents modeling and simulation studies of distillation column. This study is to stimulate sieve tray distillation (rate based model) and specifically for multiple columns process by using Aspen Hysys. The economic importance of distillation separations has been a driving force for the research in synthesis procedures for more than 30 years. Distillation accounts for almost 90% of the separation systems used in chemical process industries. The best way to reduce operating costs of existing units is to improve their efficiency and operation via process optimization and control. Simulation generates one or more trajectories (possible behaviors from the high-level model), and collects statistics from these trajectories to estimate the desired performance or dependability measures. Modeling and simulation of distillation column might already be very familiar but modeling and simulation of multicomponent distillation in multiple columns still yet being commercially introduced to the industries. In this project, the well known kind of multi components (n-butane, n-pentane and benzene) is chosen as the example to run this simulation by using multiple distillation columns. By inserting the details and specifications in Aspen Hysys, multicomponents distillation process is stimulated under steady state condition. From the result gained, calculations such as compositions, temperature, mass balance and energy balance can be done step by step. The composition, k values, temperature and flowrate will be further explained in discussion. Other than that, the limitations of steady state techniques are discussed, and the need for rigorous dynamic simulation for final selection of a workable and robust strategy is illustrated
format Undergraduates Project Papers
author Ann, Ivy Wong Fui
author_facet Ann, Ivy Wong Fui
author_sort Ann, Ivy Wong Fui
title Modeling and simulation of distillation column
title_short Modeling and simulation of distillation column
title_full Modeling and simulation of distillation column
title_fullStr Modeling and simulation of distillation column
title_full_unstemmed Modeling and simulation of distillation column
title_sort modeling and simulation of distillation column
publishDate 2014
url http://umpir.ump.edu.my/id/eprint/9020/1/Modeling%20and%20simulation%20of%20distillation%20column.pdf
http://umpir.ump.edu.my/id/eprint/9020/
_version_ 1765296902218186752
score 13.18916