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dc.contributor.authorMacháčková, Adéla
dc.contributor.authorKocich, Radim
dc.contributor.authorBojko, Marian
dc.contributor.authorKlečková, Zuzana
dc.date.accessioned2015-05-18T14:15:59Z
dc.date.available2015-05-18T14:15:59Z
dc.date.issued2015
dc.identifier.citationInternational Journal of Heat and Mass Transfer. 2015, vol. 83, p. 487-498.cs
dc.identifier.issn0017-9310
dc.identifier.issn1879-2189
dc.identifier.urihttp://hdl.handle.net/10084/106765
dc.description.abstractOur investigation was focused on possibilities of application of a secondary exchanger for use of flue gas waste heat produced by small microturbines. The investigated heat transfer system consisted of two consecutively positioned heat exchangers with various construction designs. This study brings more detailed information on heat transfer and fluid flow characteristic of the secondary exchanger and its overall influence on the efficiency of use of flue gas waste heat. Possible water condensation from the flue gas is analyzed as well. According to the results, the secondary exchanger can be utilized as the preliminary one to the primary exchanger. Consequently, the number of sections of the primary exchanger needed for water heating can be significantly decreased. Water temperature in the case of connection of both the exchangers reached 370 K. Approximately 33% of the temperature increase can be attributed to the secondary exchanger. The mean logarithmic temperature difference of the analyzed secondary exchanger was ∼166 K. The favorable geometry of the secondary exchanger resulted in a decrease in the flue gas temperature, as well as in a decrease of its gradient throughout the cross-section of the flue gas system. The flue gas temperature behind both the exchangers was sufficient to prevent condensation of water from the flue gas even under “extreme” conditions. A decrease of flue gas mass flow had a significantly higher influence on the volume of the condensed water than had lower temperature of the flue gas. A decrease of flue gas temperature by 100 K led only to formation of a more continuous layer of the condensed water on the entire length of the wall of the tube. The decreased flue gas mass flow induced change by an order of magnitude in the volume of the condensed water.cs
dc.language.isoencs
dc.publisherElseviercs
dc.relation.ispartofseriesInternational Journal of Heat and Mass Transfercs
dc.relation.urihttps://doi.org/10.1016/j.ijheatmasstransfer.2014.12.038cs
dc.rightsCopyright © 2014 Elsevier Ltd. All rights reserved.cs
dc.titleNumerical analysis of secondary heat exchanger designed for CHP units with microturbinecs
dc.typearticlecs
dc.identifier.doi10.1016/j.ijheatmasstransfer.2014.12.038
dc.type.statusPeer-reviewedcs
dc.description.sourceWeb of Sciencecs
dc.description.volume83cs
dc.description.lastpage498cs
dc.description.firstpage487cs
dc.identifier.wos000350080000048


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