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Thermal performance of one-pass shell-and-tube heat exchangers in counter-flow
dc.contributor.author | Magazoni, Felipe C. | |
dc.contributor.author | Cabezas-Gómez, Luben | |
dc.contributor.author | Fariñas Alvariño, Pablo | |
dc.contributor.author | Saiz-Jabardo, José M. | |
dc.date.accessioned | 2024-07-30T08:43:58Z | |
dc.date.available | 2024-07-30T08:43:58Z | |
dc.date.issued | 2019-02-24 | |
dc.identifier.citation | MAGAZONI, F.C., CABEZAS-GÓMEZ, L., ALVARIÑO, P.F. y SAIZ-JABARDO, J.M., 2019. THERMAL PERFORMANCE OF ONE-PASS SHELL-AND-TUBE HEAT EXCHANGERS IN COUNTER-FLOW. Brazilian Journal of Chemical Engineering [en línea], vol. 36, no. 2, pp. 869-883. ISSN 0104-6632. DOI 10.1590/0104-6632.20190362s20180424. Disponible en: https://doi.org/10.1590/0104-6632.20190362s20180424. | es_ES |
dc.identifier.issn | 0104-6632 | |
dc.identifier.uri | http://hdl.handle.net/2183/38317 | |
dc.description.abstract | [Abstract] A computational methodology is proposed and applied to calculate the temperature effectiveness, P, and the logarithmic mean temperature difference (LMTD) correction factor, F, of TEMA E shell-and-tube heat exchangers with one-pass and fluids flowing in counter-flow. An arbitrary number of baffles is considered along with three different mixture conditions of the shell-side fluid. The methodology is based on various modeling considerations adopted in several publications addressing crossflow and shell-and-tube heat exchangers. Each section between two baffles is idealized as a crossflow heat exchanger with different shell-side mixing conditions. The obtained results are compared to available solutions from the literature, showing a very good agreement. New closed-form mathematical P relations and approximate F correlations depending on the number of baffles, very appropriate for preliminary computerized analysis and design procedures, are provided. A theoretical study about the influence of the number of baffles and two shell-side fluid mixing hypotheses over P and F values is presented. The proposed methodology could be used to obtain P and F values for a particular arrangement of 1-1 shell-and-tube heat exchanger. | es_ES |
dc.description.sponsorship | The authors fully acknowledge the support provided by the Conselho Nacional de Desenvolvimento e Tecnológico (CNPq - Processes 306675/2014-5 and 304972/2017-7) and also from Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP - Process 2016/09509-1). | es_ES |
dc.description.sponsorship | Brasil. Conselho Nacional de Desenvolvimento e Tecnológico; 306675/2014-5 | es_ES |
dc.description.sponsorship | Brasil. Conselho Nacional de Desenvolvimento e Tecnológico; 304972/2017-7 | es_ES |
dc.description.sponsorship | Brasil. Fundação de Amparo à Pesquisa do Estado de São Paulo; 2016/09509-1 | es_ES |
dc.language.iso | eng | es_ES |
dc.publisher | Brazilian Society of Chemical Engineering | es_ES |
dc.relation.uri | https://doi.org/10.1590/0104-6632.20190362s20180424 | es_ES |
dc.rights | Creative Commons License Attribution-NonCommercial 4.0 International (CC BY-NC 4.0) | es_ES |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-sa/3.0/es/ | * |
dc.subject | 1-1 TEMA E shell-and-tube heat exchangers | es_ES |
dc.subject | Temperature effectiveness | es_ES |
dc.subject | LMTD correction factor | es_ES |
dc.title | Thermal performance of one-pass shell-and-tube heat exchangers in counter-flow | es_ES |
dc.type | info:eu-repo/semantics/article | es_ES |
dc.rights.access | info:eu-repo/semantics/openAccess | es_ES |
UDC.journalTitle | Brazilian Journal of Chemical Engineering | es_ES |
UDC.volume | 36 | es_ES |
UDC.issue | 2 | es_ES |
UDC.startPage | 869 | es_ES |
UDC.endPage | 883 | es_ES |
dc.identifier.doi | https://doi.org/10.1590/0104-6632.20190362s20180424 |
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