Minimization of Energy Consumption for Chemicals Ultrapurification Processes

Semiconductor industry requires ultrapure chemicals to manufacture microelectronic devices. Hydrogen peroxide is one of the most demanded chemical by the semiconductor industry and ultrapurification processes are needed to achieve the electronic grade requirements for this chemical. Among all the ul...

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Main Authors: R. Abejón, A. Garea, A. Irabien
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2012-09-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/7255
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spelling doaj-2d8718c5fc624b6088605c3d67cb9ff42021-02-22T21:02:18ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162012-09-012910.3303/CET1229259Minimization of Energy Consumption for Chemicals Ultrapurification ProcessesR. AbejónA. GareaA. IrabienSemiconductor industry requires ultrapure chemicals to manufacture microelectronic devices. Hydrogen peroxide is one of the most demanded chemical by the semiconductor industry and ultrapurification processes are needed to achieve the electronic grade requirements for this chemical. Among all the ultrapurification alternatives, reverse osmosis emerges as the most desirable option according to environmentally friendly criteria. Through modelling based on membrane transport equations and mass balances, different integrated reverse osmosis membrane cascades have been previously optimized. All the optimal solutions were characterized by the maximum allowed values for the applied pressures in the reverse osmosis stages, corresponding to the highest energy consumption and the lowest energy productivity (expressed as economic profit of the process for each unit of energy consumed). In this work, the energy productivity of the process was maximized and the optimal operation conditions were those with minimum applied pressures. However, under those conditions the membrane area required increased and the membrane productivity (expressed as economic profit of the process for each unit of membrane area employed) decreased. Therefore, multi-objective optimization was formulated to maximize simultaneously the productivities of both resources (energy and membranes).https://www.cetjournal.it/index.php/cet/article/view/7255
collection DOAJ
language English
format Article
sources DOAJ
author R. Abejón
A. Garea
A. Irabien
spellingShingle R. Abejón
A. Garea
A. Irabien
Minimization of Energy Consumption for Chemicals Ultrapurification Processes
Chemical Engineering Transactions
author_facet R. Abejón
A. Garea
A. Irabien
author_sort R. Abejón
title Minimization of Energy Consumption for Chemicals Ultrapurification Processes
title_short Minimization of Energy Consumption for Chemicals Ultrapurification Processes
title_full Minimization of Energy Consumption for Chemicals Ultrapurification Processes
title_fullStr Minimization of Energy Consumption for Chemicals Ultrapurification Processes
title_full_unstemmed Minimization of Energy Consumption for Chemicals Ultrapurification Processes
title_sort minimization of energy consumption for chemicals ultrapurification processes
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2012-09-01
description Semiconductor industry requires ultrapure chemicals to manufacture microelectronic devices. Hydrogen peroxide is one of the most demanded chemical by the semiconductor industry and ultrapurification processes are needed to achieve the electronic grade requirements for this chemical. Among all the ultrapurification alternatives, reverse osmosis emerges as the most desirable option according to environmentally friendly criteria. Through modelling based on membrane transport equations and mass balances, different integrated reverse osmosis membrane cascades have been previously optimized. All the optimal solutions were characterized by the maximum allowed values for the applied pressures in the reverse osmosis stages, corresponding to the highest energy consumption and the lowest energy productivity (expressed as economic profit of the process for each unit of energy consumed). In this work, the energy productivity of the process was maximized and the optimal operation conditions were those with minimum applied pressures. However, under those conditions the membrane area required increased and the membrane productivity (expressed as economic profit of the process for each unit of membrane area employed) decreased. Therefore, multi-objective optimization was formulated to maximize simultaneously the productivities of both resources (energy and membranes).
url https://www.cetjournal.it/index.php/cet/article/view/7255
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