Unsteady Conjugate Heat Transfer Analysis of an Immersed Particle Innovative Heat ExchangerSource: Journal of Thermal Science and Engineering Applications:;2012:;volume( 004 ):;issue: 001::page 11004DOI: 10.1115/1.4005194Publisher: The American Society of Mechanical Engineers (ASME)
Abstract: The improvement of both heat recovery Joule-Brayton cycles and closed cycle (externally fired) gas turbine plants is strongly limited by the availability of high efficiency heat exchangers. In such a scenario, a nonconventional heat exchanger was recently proposed; this device employs falling solid particles to perform heat transfer between two separate gas flows and was designed with a 1D model neglecting conduction within the particles. Although the experimental reliability of this assumption was already obtained for one particle size, there is no proof available of the quantitative effect introduced by the above mentioned simplification and, more importantly, no indication of when this assumption becomes unacceptable. In this work, direct numerical simulation (DNS) of a solid particle immersed in a gas flow has been performed in order to further validate the hypothesis of negligible conduction and to enhance the design of the proposed heat exchanger. Unsteady conjugate heat transfer has been used to predict the final temperature of the solid sphere for Reynolds numbers ranging from 30 to nearly 300, the computational grid being generated with the immersed boundary (IB) technique. A validation of the study is presented, together with grid independence and boundary independence assessment. The results fully confirmed the worthiness of the initial assumption, with a 1.4% maximum error for high Reynolds conditions (large diameter particles) with respect to the 1D model. Additionally, the code has been employed to explore the influence of the wake in the case of aligned particles, namely, the worst possible situation in terms of efficiency of the heat transfer mechanism. Finally, the discrepancy between the results obtained with an axisymmetric domain and a 3D domain, in terms of final temperature of the particle, have been investigated for the highest Reynolds number, when the flow is supposed to lose its axial symmetry.
keyword(s): Flow (Dynamics) , Temperature , Heat transfer , Particulate matter , Heat exchangers , Simulation , Heat conduction , Reynolds number AND Errors ,
|
Show full item record
| contributor author | Leonardo Nettis | |
| contributor author | Roberto Verzicco | |
| contributor author | Fabio De Bellis | |
| contributor author | Luciano A. Catalano | |
| date accessioned | 2017-05-09T00:54:34Z | |
| date available | 2017-05-09T00:54:34Z | |
| date copyright | March, 2012 | |
| date issued | 2012 | |
| identifier issn | 1948-5085 | |
| identifier other | JTSEBV-28838#011004_1.pdf | |
| identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/150299 | |
| description abstract | The improvement of both heat recovery Joule-Brayton cycles and closed cycle (externally fired) gas turbine plants is strongly limited by the availability of high efficiency heat exchangers. In such a scenario, a nonconventional heat exchanger was recently proposed; this device employs falling solid particles to perform heat transfer between two separate gas flows and was designed with a 1D model neglecting conduction within the particles. Although the experimental reliability of this assumption was already obtained for one particle size, there is no proof available of the quantitative effect introduced by the above mentioned simplification and, more importantly, no indication of when this assumption becomes unacceptable. In this work, direct numerical simulation (DNS) of a solid particle immersed in a gas flow has been performed in order to further validate the hypothesis of negligible conduction and to enhance the design of the proposed heat exchanger. Unsteady conjugate heat transfer has been used to predict the final temperature of the solid sphere for Reynolds numbers ranging from 30 to nearly 300, the computational grid being generated with the immersed boundary (IB) technique. A validation of the study is presented, together with grid independence and boundary independence assessment. The results fully confirmed the worthiness of the initial assumption, with a 1.4% maximum error for high Reynolds conditions (large diameter particles) with respect to the 1D model. Additionally, the code has been employed to explore the influence of the wake in the case of aligned particles, namely, the worst possible situation in terms of efficiency of the heat transfer mechanism. Finally, the discrepancy between the results obtained with an axisymmetric domain and a 3D domain, in terms of final temperature of the particle, have been investigated for the highest Reynolds number, when the flow is supposed to lose its axial symmetry. | |
| publisher | The American Society of Mechanical Engineers (ASME) | |
| title | Unsteady Conjugate Heat Transfer Analysis of an Immersed Particle Innovative Heat Exchanger | |
| type | Journal Paper | |
| journal volume | 4 | |
| journal issue | 1 | |
| journal title | Journal of Thermal Science and Engineering Applications | |
| identifier doi | 10.1115/1.4005194 | |
| journal fristpage | 11004 | |
| identifier eissn | 1948-5093 | |
| keywords | Flow (Dynamics) | |
| keywords | Temperature | |
| keywords | Heat transfer | |
| keywords | Particulate matter | |
| keywords | Heat exchangers | |
| keywords | Simulation | |
| keywords | Heat conduction | |
| keywords | Reynolds number AND Errors | |
| tree | Journal of Thermal Science and Engineering Applications:;2012:;volume( 004 ):;issue: 001 | |
| contenttype | Fulltext |