Flexible Design and Operation of Multi-Stage Flash (MSF) Desalination Process Subject to Variable Fouling and Variable Freshwater Demand
This work describes how the design and operation parameters of the Multi-Stage Flash (MSF) desalination process are optimised when the process is subject to variation in seawater temperature, fouling and freshwater demand throughout the day. A simple polynomial based dynamic seawater temperature and...
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doaj-1857189b9cc84e4d8c7604f7c5b0eecf2020-11-25T00:49:05ZengMDPI AGProcesses2227-97172013-10-011327929510.3390/pr1030279Flexible Design and Operation of Multi-Stage Flash (MSF) Desalination Process Subject to Variable Fouling and Variable Freshwater DemandSaid Alforjani SaidMansour EmtirIqbal M. MujtabaThis work describes how the design and operation parameters of the Multi-Stage Flash (MSF) desalination process are optimised when the process is subject to variation in seawater temperature, fouling and freshwater demand throughout the day. A simple polynomial based dynamic seawater temperature and variable freshwater demand correlations are developed based on actual data which are incorporated in the MSF mathematical model using gPROMS models builder 3.0.3. In addition, a fouling model based on stage temperature is considered. The fouling and the effect of noncondensable gases are incorporated into the calculation of overall heat transfer co-efficient for condensers. Finally, an optimisation problem is developed where the total daily operating cost of the MSF process is minimised by optimising the design (no of stages) and the operating (seawater rejected flowrate and brine recycle flowrate) parameters.http://www.mdpi.com/2227-9717/1/3/279freshwater demandstorage tankdynamic optimisationtotal operating cost |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Said Alforjani Said Mansour Emtir Iqbal M. Mujtaba |
spellingShingle |
Said Alforjani Said Mansour Emtir Iqbal M. Mujtaba Flexible Design and Operation of Multi-Stage Flash (MSF) Desalination Process Subject to Variable Fouling and Variable Freshwater Demand Processes freshwater demand storage tank dynamic optimisation total operating cost |
author_facet |
Said Alforjani Said Mansour Emtir Iqbal M. Mujtaba |
author_sort |
Said Alforjani Said |
title |
Flexible Design and Operation of Multi-Stage Flash (MSF) Desalination Process Subject to Variable Fouling and Variable Freshwater Demand |
title_short |
Flexible Design and Operation of Multi-Stage Flash (MSF) Desalination Process Subject to Variable Fouling and Variable Freshwater Demand |
title_full |
Flexible Design and Operation of Multi-Stage Flash (MSF) Desalination Process Subject to Variable Fouling and Variable Freshwater Demand |
title_fullStr |
Flexible Design and Operation of Multi-Stage Flash (MSF) Desalination Process Subject to Variable Fouling and Variable Freshwater Demand |
title_full_unstemmed |
Flexible Design and Operation of Multi-Stage Flash (MSF) Desalination Process Subject to Variable Fouling and Variable Freshwater Demand |
title_sort |
flexible design and operation of multi-stage flash (msf) desalination process subject to variable fouling and variable freshwater demand |
publisher |
MDPI AG |
series |
Processes |
issn |
2227-9717 |
publishDate |
2013-10-01 |
description |
This work describes how the design and operation parameters of the Multi-Stage Flash (MSF) desalination process are optimised when the process is subject to variation in seawater temperature, fouling and freshwater demand throughout the day. A simple polynomial based dynamic seawater temperature and variable freshwater demand correlations are developed based on actual data which are incorporated in the MSF mathematical model using gPROMS models builder 3.0.3. In addition, a fouling model based on stage temperature is considered. The fouling and the effect of noncondensable gases are incorporated into the calculation of overall heat transfer co-efficient for condensers. Finally, an optimisation problem is developed where the total daily operating cost of the MSF process is minimised by optimising the design (no of stages) and the operating (seawater rejected flowrate and brine recycle flowrate) parameters. |
topic |
freshwater demand storage tank dynamic optimisation total operating cost |
url |
http://www.mdpi.com/2227-9717/1/3/279 |
work_keys_str_mv |
AT saidalforjanisaid flexibledesignandoperationofmultistageflashmsfdesalinationprocesssubjecttovariablefoulingandvariablefreshwaterdemand AT mansouremtir flexibledesignandoperationofmultistageflashmsfdesalinationprocesssubjecttovariablefoulingandvariablefreshwaterdemand AT iqbalmmujtaba flexibledesignandoperationofmultistageflashmsfdesalinationprocesssubjecttovariablefoulingandvariablefreshwaterdemand |
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