| Project/Area Number |
02680070
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| Research Category |
Grant-in-Aid for General Scientific Research (C)
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| Allocation Type | Single-year Grants |
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| Research Field |
家政学
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| Research Institution | OSAKA CITY UNIVERSITY |
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Principal Investigator |
NAKANE Yoshikazu Osaka City University Faculty of Science of Living Professor, 生活科学部, 教授 (00047002)
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| Co-Investigator(Kenkyū-buntansha) |
DOI Tadashi Osaka City University Faculty of Science of Living Assistant, 生活科学部, 助手 (70137181)
EMURA Kazuo Osaka City University Faculty of Science of Living full time Lecturer, 生活科学部, 講師 (60138972)
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| Project Period (FY) |
1990 – 1992
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| Project Status |
Completed (Fiscal Year 1992)
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| Budget Amount *help |
¥2,200,000 (Direct Cost: ¥2,200,000)
Fiscal Year 1992: ¥500,000 (Direct Cost: ¥500,000)
Fiscal Year 1991: ¥800,000 (Direct Cost: ¥800,000)
Fiscal Year 1990: ¥900,000 (Direct Cost: ¥900,000)
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| Keywords | Wall Surface Condensation / Pattern Staining / Higher Air Tightness / Heating / Vapor Generation with Daily Life / パターン・ステイング / パタ-ン・ステイング / パタ-ンステイング |
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| Research Abstract |
We may conclude that Wall Surface Condensation is happened by the vapor generation with daily life as such as cooking, take a bath, drying the laundry and so on, and insufficiency of ventilation rate in the room.
In our former studies on the thermal boundary layer in the corner of wall, we proposed the thermal boundary layer equivalent to convective heat transfer for the practical thermal boundary layer in calculation of overall heat transmission, and classified the thermal boundary layer in the corner of wall in 10 types, and experiments by using Thermo Viewer have been undertaken under the limited condition, and, on the same conditions, numerical analysis was carried out. And empirical formula of the thermal boundary layer equivalent to convective heat transfer in each corner was obtained. In the present study, experiments by using Thermo Viewer and numerical analysis by Finite Element Method are made by applying the empirical formula of the thermal boundary layer equivalent to convective heat transfer in each corner to both internal-angled corner and external-angled corner in overall heat transmission analysis of wall corner. From the results mentioned above, we may conclude that empirical formula of the thermal boundary layer which we proposed can be applicable with united together to the numerical analysis of wall heat trans-mission by Finite Element Method.
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