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    Flow Boiling Heat Transfer of Subcooled Water on Sintered Microporous Surfaces

    Source: Journal of Heat Transfer:;2017:;volume( 139 ):;issue: 008::page 80906
    Author:
    Kim, Yeonghwan
    ,
    Kim, Junsub
    ,
    M. You, Seung
    ,
    Lee, Jungho
    ,
    Sohn, Jeong Lak
    ,
    Lee, Jungho
    DOI: 10.1115/1.4036883
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Electronic devices such as battery packs in electric vehicles and LED lights require advanced control in temperature uniformity for their optimum performance and prolonged lifetime. Flow boiling heat transfer of subcooled water (∆Tsub = 20K) in a 300 mm long minichannel with the cross section of 20×10 mm2 was investigated to improve the temperature uniformity over the entire minichannel. The minichannel was uniformity heated from the bottom copper surface. A 10 mm thick Pyrex glass was used for the top plate of the channel to visualize two-phase flow during the experiment. Microporous coating was fabricated by sintering copper particles on the top surface of the copper block. The average particle size was 50 μm, the average coating thickness was 300 μm, and the porosity was 41%, respectively. At the heat flux of 100 kW/m2, more bubbles are shown on the microporous surface compared with plain surface, resulting in better boiling heat transfer performance. These bubbles were large and stationary as liquid is evaporated and condensed to transport the heat as if heat pumps. As heat flux increases, bubble nucleation becomes more intensive, however, the larger stationary bubbles observed at 100 kW/m2 started to decrease. Most of the generated bubbles flowed through the downstream and they shrank quickly upon departure from the wall due to the 20K subcooling. High speed video showed some streaks of these small bubbles, and more streaks were observed as the heat flux increased. As shown in the left graph above, at 50 kW/m2 in subcooled flow boiling, both plain and microporous surfaces show similar local wall temperature because both are placed in the single-phase regime. In contrast, the difference of wall superheat between plain and porous surface is relatively large at higher heat flux of 500 kW/m2. Sintered microporous surface showed smaller increase in wall superheat compared with plain surface at higher wall superheat. [This study was supported by National Research Council of Science and Technology (NST) grant, Korea (Grant No. KIMM-NK203B)].
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      Flow Boiling Heat Transfer of Subcooled Water on Sintered Microporous Surfaces

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    contributor authorKim, Yeonghwan
    contributor authorKim, Junsub
    contributor authorM. You, Seung
    contributor authorLee, Jungho
    contributor authorSohn, Jeong Lak
    contributor authorLee, Jungho
    date accessioned2017-11-25T07:16:55Z
    date available2017-11-25T07:16:55Z
    date copyright2017/5/6
    date issued2017
    identifier issn0022-1481
    identifier otherht_139_08_080906.pdf
    identifier urihttp://138.201.223.254:8080/yetl1/handle/yetl/4234290
    description abstractElectronic devices such as battery packs in electric vehicles and LED lights require advanced control in temperature uniformity for their optimum performance and prolonged lifetime. Flow boiling heat transfer of subcooled water (∆Tsub = 20K) in a 300 mm long minichannel with the cross section of 20×10 mm2 was investigated to improve the temperature uniformity over the entire minichannel. The minichannel was uniformity heated from the bottom copper surface. A 10 mm thick Pyrex glass was used for the top plate of the channel to visualize two-phase flow during the experiment. Microporous coating was fabricated by sintering copper particles on the top surface of the copper block. The average particle size was 50 μm, the average coating thickness was 300 μm, and the porosity was 41%, respectively. At the heat flux of 100 kW/m2, more bubbles are shown on the microporous surface compared with plain surface, resulting in better boiling heat transfer performance. These bubbles were large and stationary as liquid is evaporated and condensed to transport the heat as if heat pumps. As heat flux increases, bubble nucleation becomes more intensive, however, the larger stationary bubbles observed at 100 kW/m2 started to decrease. Most of the generated bubbles flowed through the downstream and they shrank quickly upon departure from the wall due to the 20K subcooling. High speed video showed some streaks of these small bubbles, and more streaks were observed as the heat flux increased. As shown in the left graph above, at 50 kW/m2 in subcooled flow boiling, both plain and microporous surfaces show similar local wall temperature because both are placed in the single-phase regime. In contrast, the difference of wall superheat between plain and porous surface is relatively large at higher heat flux of 500 kW/m2. Sintered microporous surface showed smaller increase in wall superheat compared with plain surface at higher wall superheat. [This study was supported by National Research Council of Science and Technology (NST) grant, Korea (Grant No. KIMM-NK203B)].
    publisherThe American Society of Mechanical Engineers (ASME)
    titleFlow Boiling Heat Transfer of Subcooled Water on Sintered Microporous Surfaces
    typeJournal Paper
    journal volume139
    journal issue8
    journal titleJournal of Heat Transfer
    identifier doi10.1115/1.4036883
    journal fristpage80906
    journal lastpage080906-6
    treeJournal of Heat Transfer:;2017:;volume( 139 ):;issue: 008
    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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