Hydrodynamics and heat transfer in swirl flow under conditions of one-side heating. Part 1: Pressure drop and single-phase heat transfer |
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Authors: | Aleksey V. Dedov Alexander T. Komov Alexander N. Varava Victor V. Yagov |
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Affiliation: | 1. Division of Advanced Nuclear Engineering, POSTECH, Pohang 790-784, Republic of Korea;2. Department of Mechanical Engineering, POSTECH, Pohang 790-784, Republic of Korea;1. Department of Energy and Power Engineering, Ludong University, 186 Hongqi Middle Road, Yantai 264025, Shandong, China;2. School of Energy and Power Engineering, Shandong University, 17923 Jingshi Road, Jinan 250061, Shandong, China;3. School of Civil Engineering, Ludong University, 186 Hongqi Middle Road, Yantai 264025, Shandong, China;1. Institute of Advanced Energy, Kyoto Univ. Gokasho, Uji, Kyoto 611-0011, Japan;2. Department of Energy Science and Technology, Kyoto Univ. Sakyo-ku, Kyoto 606-8501, Japan;3. National Institute for Fusion Science, 322-6 Oroshi-cho, Toki, Gifu 509-5292, Japan;4. Concentration Heat and Momentum Ltd. , 3-5-4 Koji-machi, Chiyoda-ku, Tokyo 102-0083, Japan |
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Abstract: | The paper gives the basic results of experimental investigation of hydrodynamics and heat transfer in heat-absorbing devices of the ITER thermonuclear reactor, which are subjected to one-side heating. The entire array of experimental data is obtained in the following range of parameters of water flow: pressure p = 0.7–2.0 MPa, mass flux G = 340–25,000 kg/(m2 s), inlet water temperature Tin = 15–60 °C. The experiments are performed with turbulent swirl flows of water for twisted tapes with the flow swirl coefficient k = 0.90, 0.66, 0.49, 0.39, 0.25, 0.19, and 0, as well for test sections without a tape. Given in the first part of the paper are the data on pressure drop and single-phase convective heat transfer. Appropriate calculation formulas are derived, which reliably generalize the experimental data. |
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