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      https://www.riss.kr/link?id=A76266790

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      다국어 초록 (Multilingual Abstract) kakao i 다국어 번역

      A numerical study for laminar flow in the entrance region of helical tubes for uniform inlet velocity conditions is carried out by means of the finite volume method to investigate the effects of Reynolds number, pitch and curvature ratio on the flow development. This results cover a curvature ratio range of 1/10~1/320, a pitch range of 0.0~3.2, and a Reynolds number range of 125~2000. It has been found that the curvature ratio does significantly effect on the angle of flow development, but the pitch and Reynolds number do not. The characteristic angle (φc=<φ/√δ), or the non-dimensional length ?(=ι √δcos(atanλ)/d) can be used to represent the flow development for uniform inlet velocity conditions. In uniform inlet velocity conditions, the growth of boundary layer delays the flow development attributed to centrifugal force, and in which conditions the amplitude of flow oscillations is smaller than that in parabolic inlet velocity conditions. If the pitch increases or if the curvature ratio or Reynolds number decreases, the minimum friction factor and the fully developed average friction factor normalized with the friction factor of a straight tube and the flow oscillations decrease.
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      A numerical study for laminar flow in the entrance region of helical tubes for uniform inlet velocity conditions is carried out by means of the finite volume method to investigate the effects of Reynolds number, pitch and curvature ratio on the flow d...

      A numerical study for laminar flow in the entrance region of helical tubes for uniform inlet velocity conditions is carried out by means of the finite volume method to investigate the effects of Reynolds number, pitch and curvature ratio on the flow development. This results cover a curvature ratio range of 1/10~1/320, a pitch range of 0.0~3.2, and a Reynolds number range of 125~2000. It has been found that the curvature ratio does significantly effect on the angle of flow development, but the pitch and Reynolds number do not. The characteristic angle (φc=<φ/√δ), or the non-dimensional length ?(=ι √δcos(atanλ)/d) can be used to represent the flow development for uniform inlet velocity conditions. In uniform inlet velocity conditions, the growth of boundary layer delays the flow development attributed to centrifugal force, and in which conditions the amplitude of flow oscillations is smaller than that in parabolic inlet velocity conditions. If the pitch increases or if the curvature ratio or Reynolds number decreases, the minimum friction factor and the fully developed average friction factor normalized with the friction factor of a straight tube and the flow oscillations decrease.

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      참고문헌 (Reference)

      1 White, C.M., "Streamline flow through curved pipes" 123 : 645-663, 1929

      2 Patankar, S.V. et al., "Prediction of laminar flow and heat transfer in helically coiled pipes" 62 : 539-551, 1974

      3 Mishra, P., "Momentum Transfer in Curved Pipes: 1. Newtonian Fluids" 18 : 130-137, 1979

      4 Lin, C.X. et al., "Laminar forced convection in the entrance region of helical pipes" 40 : 3293-3304, 1997

      5 "Fluent 6.3 user's guide" Fluent Inc 2006

      6 Berger, S.A. et al., "Flow in curved pipes" 15 : 431-512, 1983

      7 Ito, H., "Flow in curved pipes" 30 : 543-552, 1987

      8 Austin, L.R., "Entry region for steady viscous flow in coiled circular pipes" 20 : 820-822, 1974

      9 Yao, L.S., "Entry flow in a curved pipe" 67 : 177-196, 1975

      10 Dravid, A.N. et al., "Effect of secondary fluid motion on laminar flow heat transfer in helically coiled tubes" 17 : 1114-1122, 1971

      1 White, C.M., "Streamline flow through curved pipes" 123 : 645-663, 1929

      2 Patankar, S.V. et al., "Prediction of laminar flow and heat transfer in helically coiled pipes" 62 : 539-551, 1974

      3 Mishra, P., "Momentum Transfer in Curved Pipes: 1. Newtonian Fluids" 18 : 130-137, 1979

      4 Lin, C.X. et al., "Laminar forced convection in the entrance region of helical pipes" 40 : 3293-3304, 1997

      5 "Fluent 6.3 user's guide" Fluent Inc 2006

      6 Berger, S.A. et al., "Flow in curved pipes" 15 : 431-512, 1983

      7 Ito, H., "Flow in curved pipes" 30 : 543-552, 1987

      8 Austin, L.R., "Entry region for steady viscous flow in coiled circular pipes" 20 : 820-822, 1974

      9 Yao, L.S., "Entry flow in a curved pipe" 67 : 177-196, 1975

      10 Dravid, A.N. et al., "Effect of secondary fluid motion on laminar flow heat transfer in helically coiled tubes" 17 : 1114-1122, 1971

      11 Liu, S, "Developing Convective Heat Transfer in Helical Pipes with Finite Pitch" 15 : 66-74, 1994

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      학술지 이력

      학술지 이력
      연월일 이력구분 이력상세 등재구분
      2027 평가예정 재인증평가 신청대상 (재인증)
      2021-01-01 평가 등재학술지 유지 (재인증) KCI등재
      2018-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2015-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2011-01-01 평가 등재 1차 FAIL (등재유지) KCI등재
      2009-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2006-01-01 평가 등재학술지 선정 (등재후보2차) KCI등재
      2005-06-16 학술지명변경 외국어명 : Jpurnal of Computatuonal Fluids Engineering -> Korean Society of Computatuonal Fluids Engineering KCI등재후보
      2005-01-01 평가 등재후보 1차 PASS (등재후보1차) KCI등재후보
      2004-01-01 평가 등재후보 1차 FAIL (등재후보1차) KCI등재후보
      2002-07-01 평가 등재후보학술지 선정 (신규평가) KCI등재후보
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      학술지 인용정보

      학술지 인용정보
      기준연도 WOS-KCI 통합IF(2년) KCIF(2년) KCIF(3년)
      2016 0.2 0.2 0.19
      KCIF(4년) KCIF(5년) 중심성지수(3년) 즉시성지수
      0.16 0.15 0.405 0.05
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