Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/37128
DC FieldValueLanguage
dc.contributor.authorRuiz-García, A.en_US
dc.contributor.authorFeo-García, J.en_US
dc.contributor.otherRuiz Garcia, Alejandro
dc.date.accessioned2018-05-22T11:55:51Z-
dc.date.available2018-05-22T11:55:51Z-
dc.date.issued2017en_US
dc.identifier.issn1944-3994en_US
dc.identifier.urihttp://hdl.handle.net/10553/37128-
dc.description.abstractGroundwater sources play a very important role in the Canary Islands. In fact the 80% of the reverse osmosis desalination plants in Gran Canaria are to treat brackish water. In water desalination processes, water recovery is one of the most important indexes for RO system design. But this is not always the most convenient from the point of view of the operating costs. This article aims to estimate the antiscalant/dispersant specific costs considering the maximum recovery levels for reverse osmosis systems. The products (Antiscalant A and B) have been evaluated as these sorts of products are most commonly used considering the inorganic composition of the different groundwater bodies in this island. The silica, calcium carbonate and calcium sulfate are the most commonly found salts in the groundwater of Gran Canaria. In most cases, silica had the highest effect on the antiscalant/dispersant specific costs, followed by calcium carbonate.en_US
dc.languageengen_US
dc.relation.ispartofDesalination and Water Treatmenten_US
dc.sourceDesalination and Water Treatment[ISSN 1944-3994],v. 73, p. 46-53en_US
dc.subject3308 Ingeniería y tecnología del medio ambienteen_US
dc.subject250804 Aguas subterráneasen_US
dc.subject.otherBrackish wateren_US
dc.subject.otherReverse osmosisen_US
dc.subject.otherDesalination plantsen_US
dc.subject.otherRecoveryen_US
dc.subject.otherScalingen_US
dc.subject.otherAntiscalanten_US
dc.titleAntiscalant cost and maximum water recovery in reverse osmosis for different inorganic composition of groundwateren_US
dc.typeinfo:eu-repo/semantics/Articleen_US
dc.typeinfo:eu-repo/semantics/Articlees
dc.typeArticlees
dc.identifier.doi10.5004/dwt.2017.20806
dc.identifier.scopus85020164993
dc.identifier.isi000404376700005
dcterms.isPartOfDesalination And Water Treatment
dcterms.sourceDesalination And Water Treatment[ISSN 1944-3994],v. 73, p. 46-53
dc.contributor.authorscopusid55749145800
dc.contributor.authorscopusid56925498900
dc.identifier.eissn1944-3986-
dc.description.lastpage53-
dc.description.firstpage46-
dc.relation.volume73-
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.identifier.wosWOS:000404376700005-
dc.contributor.daisngid2368242
dc.contributor.daisngid5705574
dc.identifier.investigatorRIDM-3697-2014
dc.contributor.wosstandardWOS:Ruiz-Garcia, A
dc.contributor.wosstandardWOS:Feo-Garcia, J
dc.date.coverdateAbril 2017
dc.identifier.ulpgces
item.fulltextSin texto completo-
item.grantfulltextnone-
crisitem.author.deptSistemas industriales de eficiciencia, instrumentación y protección-
crisitem.author.deptDepartamento de Ingeniería Electrónica y Automática-
crisitem.author.deptSistemas industriales de eficiciencia, instrumentación y protección-
crisitem.author.deptDepartamento de Ingeniería Electrónica y Automática-
crisitem.author.orcid0000-0002-5209-653X-
crisitem.author.parentorgDepartamento de Ingeniería Electrónica y Automática-
crisitem.author.parentorgDepartamento de Ingeniería Electrónica y Automática-
crisitem.author.fullNameRuiz García, Alejandro-
crisitem.author.fullNameFeo García, José Juan-
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