Economic assessment of a two-stage solar organic Rankine cycle for reverse osmosis desalination
The current paper presents the economic evaluation of a two-stage Solar Organic Rankine Cycle (SORC) for using the mechanical energy produced during the thermodynamic process to drive a Reverse Osmosis (RO) desalination unit. The developed integrated system is briefly analysed and the specific fresh...
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Veröffentlicht in: | Renewable energy 2009-06, Vol.34 (6), p.1579-1586 |
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description | The current paper presents the economic evaluation of a two-stage Solar Organic Rankine Cycle (SORC) for using the mechanical energy produced during the thermodynamic process to drive a Reverse Osmosis (RO) desalination unit. The developed integrated system is briefly analysed and the specific fresh water cost, as well as the cost of energy is calculated. The economic assessment results are compared with those obtained from a low-temperature SORC-RO and two alternative variants of PhotoVoltaic RO (PV–RO) systems (with and without batteries). It is found that the critical fresh water cost for the system under consideration is 7.48
€/m
3 of permeate water and the cost of energy equals to 2.74
€/kWh, when the water cost is slightly higher than the critical one (meaning 8
€/m
3). These values are considered satisfactory enough, in comparison to the other autonomous desalination technologies. Additionally, the specific fresh water cost of the developed technology was calculated to be 6.85
€/m
3, being very close to the values of the PV–RO systems. The variant of two-stage SORC significantly improves the efficiency and reduces the cost of the already developed prototype system (single-stage low-temperature SORC for RO desalination), because the specific cost is found to be much lower and taking into consideration its reliability, this technology can constitute an alternative desalination method competitive to the PV–RO on the basis of techno-economic feasibility. |
doi_str_mv | 10.1016/j.renene.2008.11.007 |
format | Article |
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€/m
3 of permeate water and the cost of energy equals to 2.74
€/kWh, when the water cost is slightly higher than the critical one (meaning 8
€/m
3). These values are considered satisfactory enough, in comparison to the other autonomous desalination technologies. Additionally, the specific fresh water cost of the developed technology was calculated to be 6.85
€/m
3, being very close to the values of the PV–RO systems. The variant of two-stage SORC significantly improves the efficiency and reduces the cost of the already developed prototype system (single-stage low-temperature SORC for RO desalination), because the specific cost is found to be much lower and taking into consideration its reliability, this technology can constitute an alternative desalination method competitive to the PV–RO on the basis of techno-economic feasibility.</description><identifier>ISSN: 0960-1481</identifier><identifier>EISSN: 1879-0682</identifier><identifier>DOI: 10.1016/j.renene.2008.11.007</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Assessments ; Cost analysis ; Cost engineering ; Desalination ; Drinking water and swimming-pool water. Desalination ; Economic assessment ; Economic data ; Economics ; Energy ; Energy economics ; Equipments, installations and applications ; Exact sciences and technology ; Fresh water ; General, economic and professional studies ; Natural energy ; Pollution ; Rankine cycle ; Reverse osmosis ; RO desalination ; Solar energy ; Solar organic Rankine cycle ; Solar thermal conversion ; Specific cost ; Water treatment and pollution</subject><ispartof>Renewable energy, 2009-06, Vol.34 (6), p.1579-1586</ispartof><rights>2008 Elsevier Ltd</rights><rights>2009 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c432t-73206edebc34ba063f5b5434ec7c5bf2b5c53b097d716c2e910f221f8105f6b33</citedby><cites>FETCH-LOGICAL-c432t-73206edebc34ba063f5b5434ec7c5bf2b5c53b097d716c2e910f221f8105f6b33</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.renene.2008.11.007$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=21252569$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Kosmadakis, G.</creatorcontrib><creatorcontrib>Manolakos, D.</creatorcontrib><creatorcontrib>Kyritsis, S.</creatorcontrib><creatorcontrib>Papadakis, G.</creatorcontrib><title>Economic assessment of a two-stage solar organic Rankine cycle for reverse osmosis desalination</title><title>Renewable energy</title><description>The current paper presents the economic evaluation of a two-stage Solar Organic Rankine Cycle (SORC) for using the mechanical energy produced during the thermodynamic process to drive a Reverse Osmosis (RO) desalination unit. The developed integrated system is briefly analysed and the specific fresh water cost, as well as the cost of energy is calculated. The economic assessment results are compared with those obtained from a low-temperature SORC-RO and two alternative variants of PhotoVoltaic RO (PV–RO) systems (with and without batteries). It is found that the critical fresh water cost for the system under consideration is 7.48
€/m
3 of permeate water and the cost of energy equals to 2.74
€/kWh, when the water cost is slightly higher than the critical one (meaning 8
€/m
3). These values are considered satisfactory enough, in comparison to the other autonomous desalination technologies. Additionally, the specific fresh water cost of the developed technology was calculated to be 6.85
€/m
3, being very close to the values of the PV–RO systems. The variant of two-stage SORC significantly improves the efficiency and reduces the cost of the already developed prototype system (single-stage low-temperature SORC for RO desalination), because the specific cost is found to be much lower and taking into consideration its reliability, this technology can constitute an alternative desalination method competitive to the PV–RO on the basis of techno-economic feasibility.</description><subject>Applied sciences</subject><subject>Assessments</subject><subject>Cost analysis</subject><subject>Cost engineering</subject><subject>Desalination</subject><subject>Drinking water and swimming-pool water. Desalination</subject><subject>Economic assessment</subject><subject>Economic data</subject><subject>Economics</subject><subject>Energy</subject><subject>Energy economics</subject><subject>Equipments, installations and applications</subject><subject>Exact sciences and technology</subject><subject>Fresh water</subject><subject>General, economic and professional studies</subject><subject>Natural energy</subject><subject>Pollution</subject><subject>Rankine cycle</subject><subject>Reverse osmosis</subject><subject>RO desalination</subject><subject>Solar energy</subject><subject>Solar organic Rankine cycle</subject><subject>Solar thermal conversion</subject><subject>Specific cost</subject><subject>Water treatment and pollution</subject><issn>0960-1481</issn><issn>1879-0682</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2009</creationdate><recordtype>article</recordtype><recordid>eNp90ctq3TAQBmBTWuhp0jfoQpteNnY0si72plBC2gYCgZKshSyPgk5tKdU4KXn7KpzQ5WEWs_lmBuZvmg_AO-Cgz_ZdwVSrE5wPHUDHuXnV7GAwY8v1IF43Oz5q3oIc4G3zjmjPOajByF1jL3xOeY2eOSIkWjFtLAfm2PY3t7S5O2SUF1dYLncuVffLpd8xIfNPfkEWcmEFH7EQskxrpkhsRnJLTG6LOZ02b4JbCN-_9JPm9vvFzfnP9ur6x-X5t6vWy15srekF1zjj5Hs5Oa77oCYle4neeDUFMSmv-omPZjagvcAReBACwgBcBT31_Unz-bD3vuQ_D0ibXSN5XBaXMD-QHfSoRilGU-WXoxKMMSCh10Oln45TWb8vRlWhPEBfMlHBYO9LXF15ssDtc0R2bw8R2eeILICtEdWxjy_7HXm3hOKSj_R_VoBQQumxuq8Hh_WDjxGLJR8xeZxjQb_ZOcfjh_4By0epPA</recordid><startdate>20090601</startdate><enddate>20090601</enddate><creator>Kosmadakis, G.</creator><creator>Manolakos, D.</creator><creator>Kyritsis, S.</creator><creator>Papadakis, G.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope><scope>7SU</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope><scope>7U6</scope><scope>F1W</scope><scope>H96</scope><scope>L.G</scope></search><sort><creationdate>20090601</creationdate><title>Economic assessment of a two-stage solar organic Rankine cycle for reverse osmosis desalination</title><author>Kosmadakis, G. ; Manolakos, D. ; Kyritsis, S. ; Papadakis, G.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c432t-73206edebc34ba063f5b5434ec7c5bf2b5c53b097d716c2e910f221f8105f6b33</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2009</creationdate><topic>Applied sciences</topic><topic>Assessments</topic><topic>Cost analysis</topic><topic>Cost engineering</topic><topic>Desalination</topic><topic>Drinking water and swimming-pool water. Desalination</topic><topic>Economic assessment</topic><topic>Economic data</topic><topic>Economics</topic><topic>Energy</topic><topic>Energy economics</topic><topic>Equipments, installations and applications</topic><topic>Exact sciences and technology</topic><topic>Fresh water</topic><topic>General, economic and professional studies</topic><topic>Natural energy</topic><topic>Pollution</topic><topic>Rankine cycle</topic><topic>Reverse osmosis</topic><topic>RO desalination</topic><topic>Solar energy</topic><topic>Solar organic Rankine cycle</topic><topic>Solar thermal conversion</topic><topic>Specific cost</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Kosmadakis, G.</creatorcontrib><creatorcontrib>Manolakos, D.</creatorcontrib><creatorcontrib>Kyritsis, S.</creatorcontrib><creatorcontrib>Papadakis, G.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><collection>Environmental Engineering Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Sustainability Science Abstracts</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy & Non-Living Resources</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><jtitle>Renewable energy</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Kosmadakis, G.</au><au>Manolakos, D.</au><au>Kyritsis, S.</au><au>Papadakis, G.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Economic assessment of a two-stage solar organic Rankine cycle for reverse osmosis desalination</atitle><jtitle>Renewable energy</jtitle><date>2009-06-01</date><risdate>2009</risdate><volume>34</volume><issue>6</issue><spage>1579</spage><epage>1586</epage><pages>1579-1586</pages><issn>0960-1481</issn><eissn>1879-0682</eissn><abstract>The current paper presents the economic evaluation of a two-stage Solar Organic Rankine Cycle (SORC) for using the mechanical energy produced during the thermodynamic process to drive a Reverse Osmosis (RO) desalination unit. The developed integrated system is briefly analysed and the specific fresh water cost, as well as the cost of energy is calculated. The economic assessment results are compared with those obtained from a low-temperature SORC-RO and two alternative variants of PhotoVoltaic RO (PV–RO) systems (with and without batteries). It is found that the critical fresh water cost for the system under consideration is 7.48
€/m
3 of permeate water and the cost of energy equals to 2.74
€/kWh, when the water cost is slightly higher than the critical one (meaning 8
€/m
3). These values are considered satisfactory enough, in comparison to the other autonomous desalination technologies. Additionally, the specific fresh water cost of the developed technology was calculated to be 6.85
€/m
3, being very close to the values of the PV–RO systems. The variant of two-stage SORC significantly improves the efficiency and reduces the cost of the already developed prototype system (single-stage low-temperature SORC for RO desalination), because the specific cost is found to be much lower and taking into consideration its reliability, this technology can constitute an alternative desalination method competitive to the PV–RO on the basis of techno-economic feasibility.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.renene.2008.11.007</doi><tpages>8</tpages></addata></record> |
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subjects | Applied sciences Assessments Cost analysis Cost engineering Desalination Drinking water and swimming-pool water. Desalination Economic assessment Economic data Economics Energy Energy economics Equipments, installations and applications Exact sciences and technology Fresh water General, economic and professional studies Natural energy Pollution Rankine cycle Reverse osmosis RO desalination Solar energy Solar organic Rankine cycle Solar thermal conversion Specific cost Water treatment and pollution |
title | Economic assessment of a two-stage solar organic Rankine cycle for reverse osmosis desalination |
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