NissirosV1, PascalFrancis, Checkpoint, bibRecord, 000006

Geothermal waters heat integration for the desalination of sea water

Identifieur interne : 000006 ( PascalFrancis/Checkpoint ); précédent : 000005; suivant : 000007

Geothermal waters heat integration for the desalination of sea water

Auteurs : C. Koroneos [Grèce] ; G. Roumbas [Grèce]

Source :

Desalination and water treatment : (Print) [ 1944-3994 ] ; 2012.

RBID : Pascal:12-0196944

Descripteurs français

Pascal (Inist)
- Dessalement, Eau mer, Distillation multiple effet, Consommation énergie, Hydrocarbure, Impact environnement, Eau douce, Cycle vie (environnement), Analyse avantage coût, Coût global, Centrale(production énergie), Centrale dessalement, Qualité eau, Energie renouvelable, Eau potable, Mer Egée, Protection environnement, Développement durable.
Wicri :
- topic : Hydrocarbure, Eau douce, Eau potable, Développement durable.

English descriptors

KwdEn :
- Aegean Sea, Cost benefit analysis, Desalination, Desalination plant, Drinking water, Energy consumption, Environment impact, Environmental protection, Fresh water, Hydrocarbon, Life cycle (environment), Life cycle cost, Multiple effect distillation, Power plant, Renewable energy, Seawater, Sustainable development, Water quality.

Abstract

The main objective of this work is to utilize the existing geothermal potential of the Greek island of Nisyros located in the southeastern part of the Aegean Sea for desalination of seawater. The technology most applicable for the exploitation of geothermal purposes is the multiple effect distillation process (MED). The exploitation of the geothermal hot water sources located in the island combined with an effective desalination technology can eliminate energy consumption from hydrocarbons, minimize the environmental impact and reduce dramatically the cost of fresh water. The determination of the overall environmental impact of the desalination plan by means of a Life Cycle Analysis, and the evaluation of the measure's economical feasibility by means of Cost-Benefit Analysis and Life Cycle Cost methods will be shown. Exergy Analysis of the process will determine its thermodynamic efficiency. This work is to determine and demonstrate the feasibility of a geothermal-driven power-desalination plant to provide high quality of water in sufficient quantity at affordable costs, while protecting the fragile island environment.

Affiliations:

Grèce

Links toward previous steps (curation, corpus...)

to stream PascalFrancis, to step Corpus: 000006
to stream PascalFrancis, to step Curation: 000034

Links to Exploration step

Pascal:12-0196944

Le document en format XML

<record><TEI><teiHeader><fileDesc><titleStmt><title xml:lang="en" level="a">Geothermal waters heat integration for the desalination of sea water</title>
<author><name sortKey="Koroneos, C" sort="Koroneos, C" uniqKey="Koroneos C" first="C." last="Koroneos">C. Koroneos</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Laboratory of Heat Transfer and Environmental Engineering, Aristotle University of Thessaloniki P.O. Box 483</s1>
<s2>Thessaloniki 54124</s2>
<s3>GRC</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Grèce</country>
<wicri:noRegion>Thessaloniki 54124</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Roumbas, G" sort="Roumbas, G" uniqKey="Roumbas G" first="G." last="Roumbas">G. Roumbas</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Laboratory of Heat Transfer and Environmental Engineering, Aristotle University of Thessaloniki P.O. Box 483</s1>
<s2>Thessaloniki 54124</s2>
<s3>GRC</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Grèce</country>
<wicri:noRegion>Thessaloniki 54124</wicri:noRegion>
</affiliation>
</author>
</titleStmt>
<publicationStmt><idno type="wicri:source">INIST</idno>
<idno type="inist">12-0196944</idno>
<date when="2012">2012</date>
<idno type="stanalyst">PASCAL 12-0196944 INIST</idno>
<idno type="RBID">Pascal:12-0196944</idno>
<idno type="wicri:Area/PascalFrancis/Corpus">000006</idno>
<idno type="wicri:Area/PascalFrancis/Curation">000034</idno>
<idno type="wicri:Area/PascalFrancis/Checkpoint">000006</idno>
<idno type="wicri:explorRef" wicri:stream="PascalFrancis" wicri:step="Checkpoint">000006</idno>
</publicationStmt>
<sourceDesc><biblStruct><analytic><title xml:lang="en" level="a">Geothermal waters heat integration for the desalination of sea water</title>
<author><name sortKey="Koroneos, C" sort="Koroneos, C" uniqKey="Koroneos C" first="C." last="Koroneos">C. Koroneos</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Laboratory of Heat Transfer and Environmental Engineering, Aristotle University of Thessaloniki P.O. Box 483</s1>
<s2>Thessaloniki 54124</s2>
<s3>GRC</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Grèce</country>
<wicri:noRegion>Thessaloniki 54124</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Roumbas, G" sort="Roumbas, G" uniqKey="Roumbas G" first="G." last="Roumbas">G. Roumbas</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Laboratory of Heat Transfer and Environmental Engineering, Aristotle University of Thessaloniki P.O. Box 483</s1>
<s2>Thessaloniki 54124</s2>
<s3>GRC</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Grèce</country>
<wicri:noRegion>Thessaloniki 54124</wicri:noRegion>
</affiliation>
</author>
</analytic>
<series><title level="j" type="main">Desalination and water treatment : (Print)</title>
<title level="j" type="abbreviated">Desalination water treat. : (Print)</title>
<idno type="ISSN">1944-3994</idno>
<imprint><date when="2012">2012</date>
</imprint>
</series>
</biblStruct>
</sourceDesc>
<seriesStmt><title level="j" type="main">Desalination and water treatment : (Print)</title>
<title level="j" type="abbreviated">Desalination water treat. : (Print)</title>
<idno type="ISSN">1944-3994</idno>
</seriesStmt>
</fileDesc>
<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Aegean Sea</term>
<term>Cost benefit analysis</term>
<term>Desalination</term>
<term>Desalination plant</term>
<term>Drinking water</term>
<term>Energy consumption</term>
<term>Environment impact</term>
<term>Environmental protection</term>
<term>Fresh water</term>
<term>Hydrocarbon</term>
<term>Life cycle (environment)</term>
<term>Life cycle cost</term>
<term>Multiple effect distillation</term>
<term>Power plant</term>
<term>Renewable energy</term>
<term>Seawater</term>
<term>Sustainable development</term>
<term>Water quality</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr"><term>Dessalement</term>
<term>Eau mer</term>
<term>Distillation multiple effet</term>
<term>Consommation énergie</term>
<term>Hydrocarbure</term>
<term>Impact environnement</term>
<term>Eau douce</term>
<term>Cycle vie (environnement)</term>
<term>Analyse avantage coût</term>
<term>Coût global</term>
<term>Centrale(production énergie)</term>
<term>Centrale dessalement</term>
<term>Qualité eau</term>
<term>Energie renouvelable</term>
<term>Eau potable</term>
<term>Mer Egée</term>
<term>Protection environnement</term>
<term>Développement durable</term>
</keywords>
<keywords scheme="Wicri" type="topic" xml:lang="fr"><term>Hydrocarbure</term>
<term>Eau douce</term>
<term>Eau potable</term>
<term>Développement durable</term>
</keywords>
</textClass>
</profileDesc>
</teiHeader>
<front><div type="abstract" xml:lang="en">The main objective of this work is to utilize the existing geothermal potential of the Greek island of Nisyros located in the southeastern part of the Aegean Sea for desalination of seawater. The technology most applicable for the exploitation of geothermal purposes is the multiple effect distillation process (MED). The exploitation of the geothermal hot water sources located in the island combined with an effective desalination technology can eliminate energy consumption from hydrocarbons, minimize the environmental impact and reduce dramatically the cost of fresh water. The determination of the overall environmental impact of the desalination plan by means of a Life Cycle Analysis, and the evaluation of the measure's economical feasibility by means of Cost-Benefit Analysis and Life Cycle Cost methods will be shown. Exergy Analysis of the process will determine its thermodynamic efficiency. This work is to determine and demonstrate the feasibility of a geothermal-driven power-desalination plant to provide high quality of water in sufficient quantity at affordable costs, while protecting the fragile island environment.</div>
</front>
</TEI>
<inist><standard h6="B"><pA><fA01 i1="01" i2="1"><s0>1944-3994</s0>
</fA01>
<fA03 i2="1"><s0>Desalination water treat. : (Print)</s0>
</fA03>
<fA05><s2>37</s2>
</fA05>
<fA06><s2>1-3</s2>
</fA06>
<fA08 i1="01" i2="1" l="ENG"><s1>Geothermal waters heat integration for the desalination of sea water</s1>
</fA08>
<fA11 i1="01" i2="1"><s1>KORONEOS (C.)</s1>
</fA11>
<fA11 i1="02" i2="1"><s1>ROUMBAS (G.)</s1>
</fA11>
<fA14 i1="01"><s1>Laboratory of Heat Transfer and Environmental Engineering, Aristotle University of Thessaloniki P.O. Box 483</s1>
<s2>Thessaloniki 54124</s2>
<s3>GRC</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</fA14>
<fA20><s1>69-76</s1>
</fA20>
<fA21><s1>2012</s1>
</fA21>
<fA23 i1="01"><s0>ENG</s0>
</fA23>
<fA43 i1="01"><s1>INIST</s1>
<s2>28018</s2>
<s5>354000509267170090</s5>
</fA43>
<fA44><s0>0000</s0>
<s1>© 2012 INIST-CNRS. All rights reserved.</s1>
</fA44>
<fA45><s0>16 ref.</s0>
</fA45>
<fA47 i1="01" i2="1"><s0>12-0196944</s0>
</fA47>
<fA60><s1>P</s1>
</fA60>
<fA61><s0>A</s0>
</fA61>
<fA64 i1="01" i2="1"><s0>Desalination and water treatment : (Print)</s0>
</fA64>
<fA66 i1="01"><s0>ITA</s0>
</fA66>
<fC01 i1="01" l="ENG"><s0>The main objective of this work is to utilize the existing geothermal potential of the Greek island of Nisyros located in the southeastern part of the Aegean Sea for desalination of seawater. The technology most applicable for the exploitation of geothermal purposes is the multiple effect distillation process (MED). The exploitation of the geothermal hot water sources located in the island combined with an effective desalination technology can eliminate energy consumption from hydrocarbons, minimize the environmental impact and reduce dramatically the cost of fresh water. The determination of the overall environmental impact of the desalination plan by means of a Life Cycle Analysis, and the evaluation of the measure's economical feasibility by means of Cost-Benefit Analysis and Life Cycle Cost methods will be shown. Exergy Analysis of the process will determine its thermodynamic efficiency. This work is to determine and demonstrate the feasibility of a geothermal-driven power-desalination plant to provide high quality of water in sufficient quantity at affordable costs, while protecting the fragile island environment.</s0>
</fC01>
<fC02 i1="01" i2="X"><s0>001D16A</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE"><s0>Dessalement</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG"><s0>Desalination</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA"><s0>Desaladura</s0>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE"><s0>Eau mer</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG"><s0>Seawater</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA"><s0>Agua mar</s0>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE"><s0>Distillation multiple effet</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Multiple effect distillation</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA"><s0>Destilación efecto múltiple</s0>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE"><s0>Consommation énergie</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG"><s0>Energy consumption</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Consumo energía</s0>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Hydrocarbure</s0>
<s2>FX</s2>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>Hydrocarbon</s0>
<s2>FX</s2>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>Hidrocarburo</s0>
<s2>FX</s2>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Impact environnement</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Environment impact</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Impacto medio ambiente</s0>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Eau douce</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Fresh water</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Agua dulce</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Cycle vie (environnement)</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Life cycle (environment)</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Ciclo vida (medio ambiente)</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Analyse avantage coût</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Cost benefit analysis</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Análisis coste beneficio</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Coût global</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Life cycle cost</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Costo global</s0>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Centrale(production énergie)</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Power plant</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Central eléctrica</s0>
<s5>11</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Centrale dessalement</s0>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Desalination plant</s0>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Central desaladura</s0>
<s5>12</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Qualité eau</s0>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Water quality</s0>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Calidad agua</s0>
<s5>13</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE"><s0>Energie renouvelable</s0>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG"><s0>Renewable energy</s0>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA"><s0>Energía renovable</s0>
<s5>14</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE"><s0>Eau potable</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="ENG"><s0>Drinking water</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="SPA"><s0>Agua potable</s0>
<s5>15</s5>
</fC03>
<fC03 i1="16" i2="X" l="FRE"><s0>Mer Egée</s0>
<s2>NG</s2>
<s5>31</s5>
</fC03>
<fC03 i1="16" i2="X" l="ENG"><s0>Aegean Sea</s0>
<s2>NG</s2>
<s5>31</s5>
</fC03>
<fC03 i1="16" i2="X" l="SPA"><s0>Mar Egeo</s0>
<s2>NG</s2>
<s5>31</s5>
</fC03>
<fC03 i1="17" i2="X" l="FRE"><s0>Protection environnement</s0>
<s5>35</s5>
</fC03>
<fC03 i1="17" i2="X" l="ENG"><s0>Environmental protection</s0>
<s5>35</s5>
</fC03>
<fC03 i1="17" i2="X" l="SPA"><s0>Protección medio ambiente</s0>
<s5>35</s5>
</fC03>
<fC03 i1="18" i2="X" l="FRE"><s0>Développement durable</s0>
<s5>36</s5>
</fC03>
<fC03 i1="18" i2="X" l="ENG"><s0>Sustainable development</s0>
<s5>36</s5>
</fC03>
<fC03 i1="18" i2="X" l="SPA"><s0>Desarrollo sostenible</s0>
<s5>36</s5>
</fC03>
<fC07 i1="01" i2="X" l="FRE"><s0>Mer Méditerranée</s0>
<s2>NG</s2>
</fC07>
<fC07 i1="01" i2="X" l="ENG"><s0>Mediterranean Sea</s0>
<s2>NG</s2>
</fC07>
<fC07 i1="01" i2="X" l="SPA"><s0>Mar Mediterráneo</s0>
<s2>NG</s2>
</fC07>
<fC07 i1="02" i2="X" l="FRE"><s0>Composé organique</s0>
<s2>NA</s2>
<s5>43</s5>
</fC07>
<fC07 i1="02" i2="X" l="ENG"><s0>Organic compounds</s0>
<s2>NA</s2>
<s5>43</s5>
</fC07>
<fC07 i1="02" i2="X" l="SPA"><s0>Compuesto orgánico</s0>
<s2>NA</s2>
<s5>43</s5>
</fC07>
<fN21><s1>156</s1>
</fN21>
<fN44 i1="01"><s1>OTO</s1>
</fN44>
<fN82><s1>OTO</s1>
</fN82>
</pA>
</standard>
</inist>
<affiliations><list><country><li>Grèce</li>
</country>
</list>
<tree><country name="Grèce"><noRegion><name sortKey="Koroneos, C" sort="Koroneos, C" uniqKey="Koroneos C" first="C." last="Koroneos">C. Koroneos</name>
</noRegion>
<name sortKey="Roumbas, G" sort="Roumbas, G" uniqKey="Roumbas G" first="G." last="Roumbas">G. Roumbas</name>
</country>
</tree>
</affiliations>
</record>

Pour manipuler ce document sous Unix (Dilib)

EXPLOR_STEP=$WICRI_ROOT/Wicri/Terre/explor/NissirosV1/Data/PascalFrancis/Checkpoint

HfdSelect -h $EXPLOR_STEP/biblio.hfd -nk 000006 | SxmlIndent | more

HfdSelect -h $EXPLOR_AREA/Data/PascalFrancis/Checkpoint/biblio.hfd -nk 000006 | SxmlIndent | more

Pour mettre un lien sur cette page dans le réseau Wicri

{{Explor lien
   |wiki=    Wicri/Terre
   |area=    NissirosV1
   |flux=    PascalFrancis
   |étape=   Checkpoint
   |type=    RBID
   |clé=     Pascal:12-0196944
   |texte=   Geothermal waters heat integration for the desalination of sea water
}}

This area was generated with Dilib version V0.6.33.
Data generation: Tue Jan 16 00:18:27 2018. Site generation: Mon Feb 1 22:09:13 2021

	Serveur d'exploration Nissiros
	Attention, ce site est en cours de développement ! Attention, site généré par des moyens informatiques à partir de corpus bruts. Les informations ne sont donc pas validées.

Serveur d'exploration Nissiros

Geothermal waters heat integration for the desalination of sea water

Geothermal waters heat integration for the desalination of sea water

Source :

Descripteurs français

English descriptors

Abstract

Links toward previous steps (curation, corpus...)

Links to Exploration step

Le document en format XML

Pour manipuler ce document sous Unix (Dilib)

Pour mettre un lien sur cette page dans le réseau Wicri