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    Improving the Thermofluid Performance of a Shell and Corrugated Coil Heat Exchanger With Novel Configurations

    Source: Journal of Thermal Science and Engineering Applications:;2026:;volume( 018 ):;issue:009
    Author:
    Abdelmagied, Mahmoud M.
    DOI: 10.1115/1.4071053
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Abstract. In the current investigation, novel coil configurations of a shell and corrugated coil heat exchanger (SCCHX) were experimentally examined and compared with the conventional shell and smooth coil heat exchanger (SSCHX). The innovative coil design enhances the disruption of the thermal boundary layer by increasing the fluid mixing by the curved coil and the corrugation compared to conventional helical designs. This geometry promotes better fluid mixing near the coil surface, resulting in a more uniform temperature distribution, reduced temperature polarization, and a higher temperature difference between the coil and the surrounding fluid. The influence of coil configuration, inclination angle, and Reynolds number on the thermofluid performance was examined. Six curved coils were designed and fabricated for this investigation. Three smooth configurations—model A (divergent–convergent design), model B (convergent–divergent design), and model C (traditional helical design) as well as three corrugated configurations were tested. The experiments were conducted at inclination angles of 0 deg, 45 deg, and 90 deg. The experimental runs covered a range of Dean number of 2000 ≤ Dni ≤ 12,400, corresponding to mass flow rates of 0.032 ≤ ṁi ≤ 0.18 kg/s on the coil side and 0.067 ≤ ṁsh ≤ 0.175 kg/s on the shell side. The new coil configurations showed significant enhancements in the Nusselt number (Nui) by 67.8% and 34.2% for the smooth configurations (models A and B) compared with model C, and by 65.7% and 30.2% for the corrugated configurations at an inclination angle of 90 deg. Conversely, the new coil configurations increased the friction factor (fi) by 26.7% and 50.4% for the smooth configurations (models A and B) compared with model C, and by 21.4% and 31.1% for the corrugated configurations at 90 deg. In addition, the inclination angle of 90 deg recorded the highest thermal performance among all inclination angles, albeit at the expense of higher pressure drop. The maximum thermal performance index (TPI), values of 2.75, 2.6, and 2.5 were obtained for models A, B, and C, respectively, at an inclination angle of 90 deg.
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      Improving the Thermofluid Performance of a Shell and Corrugated Coil Heat Exchanger With Novel Configurations

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    https://yetl.yabesh.ir/yetl1/handle/yetl/4315394
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    contributor authorAbdelmagied, Mahmoud M.
    date accessioned2026-08-23T07:38:54Z
    date available2026-08-23T07:38:54Z
    date copyright2026/09/01
    date issued2026
    identifier issn1948-5085
    identifier othertsea-25-1686.pdf
    identifier urihttp://yetl.yabesh.ir/yetl1/handle/yetl/4315394
    description abstractAbstract. In the current investigation, novel coil configurations of a shell and corrugated coil heat exchanger (SCCHX) were experimentally examined and compared with the conventional shell and smooth coil heat exchanger (SSCHX). The innovative coil design enhances the disruption of the thermal boundary layer by increasing the fluid mixing by the curved coil and the corrugation compared to conventional helical designs. This geometry promotes better fluid mixing near the coil surface, resulting in a more uniform temperature distribution, reduced temperature polarization, and a higher temperature difference between the coil and the surrounding fluid. The influence of coil configuration, inclination angle, and Reynolds number on the thermofluid performance was examined. Six curved coils were designed and fabricated for this investigation. Three smooth configurations—model A (divergent–convergent design), model B (convergent–divergent design), and model C (traditional helical design) as well as three corrugated configurations were tested. The experiments were conducted at inclination angles of 0 deg, 45 deg, and 90 deg. The experimental runs covered a range of Dean number of 2000 ≤ Dni ≤ 12,400, corresponding to mass flow rates of 0.032 ≤ ṁi ≤ 0.18 kg/s on the coil side and 0.067 ≤ ṁsh ≤ 0.175 kg/s on the shell side. The new coil configurations showed significant enhancements in the Nusselt number (Nui) by 67.8% and 34.2% for the smooth configurations (models A and B) compared with model C, and by 65.7% and 30.2% for the corrugated configurations at an inclination angle of 90 deg. Conversely, the new coil configurations increased the friction factor (fi) by 26.7% and 50.4% for the smooth configurations (models A and B) compared with model C, and by 21.4% and 31.1% for the corrugated configurations at 90 deg. In addition, the inclination angle of 90 deg recorded the highest thermal performance among all inclination angles, albeit at the expense of higher pressure drop. The maximum thermal performance index (TPI), values of 2.75, 2.6, and 2.5 were obtained for models A, B, and C, respectively, at an inclination angle of 90 deg.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleImproving the Thermofluid Performance of a Shell and Corrugated Coil Heat Exchanger With Novel Configurations
    typeJournal Paper
    journal volume18
    journal issue9
    journal titleJournal of Thermal Science and Engineering Applications
    identifier doi10.1115/1.4071053
    treeJournal of Thermal Science and Engineering Applications:;2026:;volume( 018 ):;issue:009
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
    نرم افزار کتابخانه دیجیتال "دی اسپیس" فارسی شده توسط یابش برای کتابخانه های ایرانی | تماس با یابش
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