Process intensification of seawater reverse osmosis through enhanced train capacity and module size - Simulation on Lanzarote IV SWRO plant

Process intensification on seawater reverse osmosis (SWRO) plant can be realized through the increase of both train capacity and module size. The investigations were conducted based on a two-staged medium-sized (capacity of 25,000 m3/day) SWRO plant, Lanzarote IV, Canary Island. Comparison between a...

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Main Authors: Haryati, S., Hamzah, A. B., Goh, P. S., Abdullah, M. S., Ismail, A. F., Bustan, M. D.
Format: Article
Published: Elsevier B.V. 2017
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Online Access:http://eprints.utm.my/id/eprint/76083/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85009911278&doi=10.1016%2fj.desal.2017.01.011&partnerID=40&md5=07e0a579263984744c363264f7f1ad1b
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spelling my.utm.760832019-02-19T04:21:49Z http://eprints.utm.my/id/eprint/76083/ Process intensification of seawater reverse osmosis through enhanced train capacity and module size - Simulation on Lanzarote IV SWRO plant Haryati, S. Hamzah, A. B. Goh, P. S. Abdullah, M. S. Ismail, A. F. Bustan, M. D. TP Chemical technology Process intensification on seawater reverse osmosis (SWRO) plant can be realized through the increase of both train capacity and module size. The investigations were conducted based on a two-staged medium-sized (capacity of 25,000 m3/day) SWRO plant, Lanzarote IV, Canary Island. Comparison between all-16-inch (first and second stages with GE Osmonics' AE-1600 and AG-1600, respectively) and mixed (only the first stage fitted with 16-inch) pressure vessels (PV) was also discussed herein. Exergy and exergoeconomic analysis was performed to calculate specific energy consumption (SEC), effergy and water costs. ROSA 9.1 (for 8-inch diameter modules) and Winflows 3.2 (for 16-inch diameter modules) were utilized to obtain energetic and technical data. The analysis revealed that the incorporation of all-16-inch modules on Lanzarote IV allowed more versatile train size design. The availability of the train was not the sole determining factor for the total cost of 16-inch PV-based configurations since the membrane capital cost only constitutes 2–3% of the total cost. In fact, the simultaneous increase in both train size and PV diameter can significantly offer operational advantages in term of technical, economical and plant footprint for a medium-size SWRO plant. Elsevier B.V. 2017 Article PeerReviewed Haryati, S. and Hamzah, A. B. and Goh, P. S. and Abdullah, M. S. and Ismail, A. F. and Bustan, M. D. (2017) Process intensification of seawater reverse osmosis through enhanced train capacity and module size - Simulation on Lanzarote IV SWRO plant. Desalination, 408 . pp. 92-101. ISSN 0011-9164 https://www.scopus.com/inward/record.uri?eid=2-s2.0-85009911278&doi=10.1016%2fj.desal.2017.01.011&partnerID=40&md5=07e0a579263984744c363264f7f1ad1b
institution Universiti Teknologi Malaysia
building UTM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Malaysia
content_source UTM Institutional Repository
url_provider http://eprints.utm.my/
topic TP Chemical technology
spellingShingle TP Chemical technology
Haryati, S.
Hamzah, A. B.
Goh, P. S.
Abdullah, M. S.
Ismail, A. F.
Bustan, M. D.
Process intensification of seawater reverse osmosis through enhanced train capacity and module size - Simulation on Lanzarote IV SWRO plant
description Process intensification on seawater reverse osmosis (SWRO) plant can be realized through the increase of both train capacity and module size. The investigations were conducted based on a two-staged medium-sized (capacity of 25,000 m3/day) SWRO plant, Lanzarote IV, Canary Island. Comparison between all-16-inch (first and second stages with GE Osmonics' AE-1600 and AG-1600, respectively) and mixed (only the first stage fitted with 16-inch) pressure vessels (PV) was also discussed herein. Exergy and exergoeconomic analysis was performed to calculate specific energy consumption (SEC), effergy and water costs. ROSA 9.1 (for 8-inch diameter modules) and Winflows 3.2 (for 16-inch diameter modules) were utilized to obtain energetic and technical data. The analysis revealed that the incorporation of all-16-inch modules on Lanzarote IV allowed more versatile train size design. The availability of the train was not the sole determining factor for the total cost of 16-inch PV-based configurations since the membrane capital cost only constitutes 2–3% of the total cost. In fact, the simultaneous increase in both train size and PV diameter can significantly offer operational advantages in term of technical, economical and plant footprint for a medium-size SWRO plant.
format Article
author Haryati, S.
Hamzah, A. B.
Goh, P. S.
Abdullah, M. S.
Ismail, A. F.
Bustan, M. D.
author_facet Haryati, S.
Hamzah, A. B.
Goh, P. S.
Abdullah, M. S.
Ismail, A. F.
Bustan, M. D.
author_sort Haryati, S.
title Process intensification of seawater reverse osmosis through enhanced train capacity and module size - Simulation on Lanzarote IV SWRO plant
title_short Process intensification of seawater reverse osmosis through enhanced train capacity and module size - Simulation on Lanzarote IV SWRO plant
title_full Process intensification of seawater reverse osmosis through enhanced train capacity and module size - Simulation on Lanzarote IV SWRO plant
title_fullStr Process intensification of seawater reverse osmosis through enhanced train capacity and module size - Simulation on Lanzarote IV SWRO plant
title_full_unstemmed Process intensification of seawater reverse osmosis through enhanced train capacity and module size - Simulation on Lanzarote IV SWRO plant
title_sort process intensification of seawater reverse osmosis through enhanced train capacity and module size - simulation on lanzarote iv swro plant
publisher Elsevier B.V.
publishDate 2017
url http://eprints.utm.my/id/eprint/76083/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85009911278&doi=10.1016%2fj.desal.2017.01.011&partnerID=40&md5=07e0a579263984744c363264f7f1ad1b
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