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<dc:title xml:lang="pl"><![CDATA[Parametric Investigation of an Assessed Subcritical Dual-Pressure Evaporation Organic Rankine Cycles Based on Different Heat Source Temperatures]]></dc:title>
<dc:creator><![CDATA[Rowshanaie, Omid]]></dc:creator>
<dc:creator><![CDATA[Mohd Tohir, Mohd Zahirasri]]></dc:creator>
<dc:creator><![CDATA[Rowshanaie, Hooman]]></dc:creator>
<dc:subject xml:lang="pl"><![CDATA[assessment process]]></dc:subject>
<dc:subject xml:lang="pl"><![CDATA[dual-pressure evaporation Organic Rankine Cycle (ORC)]]></dc:subject>
<dc:subject xml:lang="pl"><![CDATA[maximum net power output]]></dc:subject>
<dc:subject xml:lang="pl"><![CDATA[first and second law of efficiencies]]></dc:subject>
<dc:description xml:lang="pl"><![CDATA[The dual-pressure evaporation Organic Rankine Cycle (ORC) consists of two compression processes, two evaporation processes, and two expansion processes, and is becoming more prevalent than single-pressure evaporation ORCs due to its higher performance and maximum net power output. This study investigates different heat sources analysis in a simulated parametric dual-pressure evaporation ORC according to the assessment design process.]]></dc:description>
<dc:description xml:lang="pl"><![CDATA[The current dual-pressure evaporation ORC makes a comparison between R245fa, an old refrigerant, and R1233zd(E), a substitute for R245fa, as working fluids, paying attention to three water temperatures (100, 125, and 150 [degrees]C) as a heat source to generate maximum net power output. Based on designing an assessment process for dual-pressure evaporation ORC at 100 [degrees]C and 125 °C heat sources, R1233zd(E) is compared with R245fa, revealing an improvement of 9.58 kW and 16.14 kW in maximum net power output.]]></dc:description>
<dc:description xml:lang="pl"><![CDATA[Furthermore, according to the first and second laws of efficiency, R1233zd(E) exhibits improvements of 0.09% and 0.56%, as well as 0.15% and 1.04%, respectively. The pressure rise in low and high-pressure compression processes, parallel with a higher exergy flow rate in evaporation processes of R1233zd(E), demonstrates a direct and positive influence with a maximum net power output. At 150 [degrees]C, the power generated by the lower-pressure turbine improved by 28.1 kW in R1233zd(E) compared with R245fa.]]></dc:description>
<dc:publisher><![CDATA[Zielona Góra: Uniwersytet Zielonogórski]]></dc:publisher>
<dc:contributor><![CDATA[Jurczak, Paweł - red.]]></dc:contributor>
<dc:date><![CDATA[2026]]></dc:date>
<dc:type xml:lang="pl"><![CDATA[artykuł]]></dc:type>
<dc:format xml:lang="pl"><![CDATA[application/pdf]]></dc:format>
<dc:identifier><![CDATA[http://zbc.uz.zgora.pl/Content/98857/Volume31_Issue3_paper_07.pdf]]></dc:identifier>
<dc:identifier><![CDATA[https://zbc.uz.zgora.pl/dlibra/publication/115109/edition/98857/content]]></dc:identifier>
<dc:identifier><![CDATA[oai:zbc.uz.zgora.pl:98857]]></dc:identifier>
<dc:source xml:lang="pl"><![CDATA[IJAME, volume 31, number 3 (2026)]]></dc:source>
<dc:language><![CDATA[eng]]></dc:language>
<dc:relation><![CDATA[oai:zbc.uz.zgora.pl:publication:115109]]></dc:relation>
<dc:rights xml:lang="pl"><![CDATA[CC 4.0]]></dc:rights>
<dc:rights xml:lang="pl"><![CDATA[Biblioteka Uniwersytetu Zielonogórskiego]]></dc:rights>
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