• Title/Summary/Keyword: 2 벽면 수축채널

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Enhanced heat transfer in the convergent rectangular channels with ∧/∨-shaped ribs on one wall (한 면에 ∧/∨형 리브가 있는 2벽면 수축 사각채널의 열전달 증가)

  • Lee, Myung-Sung;Yu, Ji-Ui;Jeong, Hee-Jae;Choi, Dong-Geun;Ha, Dong-Jun;Go, Jin-Su;Ahn, Soo-Whan
    • Journal of Advanced Marine Engineering and Technology
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    • v.40 no.4
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    • pp.270-274
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    • 2016
  • The effect of the rib angle-of-attack on heat transfer in the convergent channel with ${\vee}/{\wedge}$-shaped ribs was examined experimentally. Four differently angled ribs (a = $30^{\circ}$, $45^{\circ}$, $60^{\circ}$, and $90^{\circ}$) were placed to only the one sided wall. The ribbed wall was manufactured with a fixed rib height (e) of 10 mm and rib spacing (p)-to-height (e) ratio of 10. The convergent channel had a length of 1,000 mm and a cross-sectional areas of $100mm{\times}100mm$ at inlet and $50mm{\times}100mm$ at exit. The measurement was conducted for the Reynolds numbers ranging from 22,000 to 75,000. The results show that the Nusselt number is generally higher at higher Reynolds number and that an angle-of-attack of $45^{\circ}$ at the ${\wedge}$-shaped rib produces the greatest Nusselt number.

Effect of Inclined Wall Number on Heat Transfer and Friction in the Smooth Channel (매끈한 사각채널에서 경사 벽면 수가 열전달과 마찰에 미치는 효과)

  • Lee, Myung-Sung;Ahn, Soo-Whan
    • Journal of Power System Engineering
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    • v.18 no.3
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    • pp.66-72
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    • 2014
  • The local heat transfer and pressure drop of developed turbulent flows in the smooth convergent/divergent channels with rectangular and square cross-sectional areas along the axial distance have been investigated experimentally. The measurement was conducted within the range of Reynolds numbers from 15,000 to 89,000. The channel hydraulic diameter ratios of 0.67 and 1.49 in the rectangular channel with 2 inclined walls and the ratios 0.75 and 1.33 in the square channel with 4 inclined walls are considered. The comparison showed that among the four channels the square divergent channel has the highest thermal performance at the identical mass flow rate, at the identical pumping power, and at the static pressure drop.