Development of Numerical Experimental Model for Heat Transfer in High Quality Region of Flow Boiling in Tube Evaporator with Twisted Tape-Insert
Development of Numerical Experimental Model for Heat Transfer in High Quality Region of Flow Boiling in Tube Evaporator with Twisted Tape-Insert
批准号:
10650216
负责人:
YOSHIDA Keisuke
金额:
$2.11万
依托单位:
依托单位国家:
日本
项目类别:
Grant-in-Aid for Scientific Research (C)
财政年份:
1998
资助国家:
日本
项目状态:
已结题
起止时间:
1998 至 1999
中文摘要
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英文摘要
This research aimed to develop a numerical experimental mode which can simulates behavior of droplets in the post-dryout region of flow boiling in tube evaporator, in order to find the way to the heat transfer enhancement in this region effectively by twisted tape-insert, which contributes to reducing the tube length required. The research was performed by experimental studies on heat transfer and critical heat flux(CHF)of the flow boiling, and by numerical analysis using computer.In the experiments data for refrigerant HFC134a were obtained for the horizontal flow conditions (mass flux 100-600 kg/mィイD12ィエD1s). The following results were clarified : (1)The heat transfer characteristics and the relation between CHF and the critical quality for a smooth tube(O. D. 7mm, I. D. 6.34mm)showed the similar tendencies to the results which had been obtained previously for the different flow conditions and refrigerants by the investigators. (2)Magnitude of the heat transfer enhancement by the twi … More sted tape inserted into the smooth tube in the post-dryout region agreed qualitatively with the experimental results which had been obtained for refrigerant CHF113 by the head investigator.In the numerical analysis a simulation of behavior of a single droplet in vapor flow which collides with heated wall was carried out by the modified VOF method which is taking account of phase change at the vapor-liquid interface. The results showed that the calculation could simulate behavior of the droplet until it collided with the wall, and the definition of temperature of the cell which included the interface affected the complexity of calculation beyond the investigators' expectation. However the most relevant condition at which the droplet departs form the wall has not been found.In addition, a simple method using Thermo-Paint(temperature sensing paint), which changes its color with temperature, was proposed to measure the surface temperature profile outside the tube, and was confirmed its usefulness by another experiment. Less
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H. Mori: "Dryout Quality and Post-Dryout Heat Transfer Coefficient for a Refrigerant Flowing in Horizontal Evaporator Tubes"20th Int. Congress of refrigeration. (in press). (2000)
H. Mori:“水平蒸发器管中流动的制冷剂的干燥质量和干燥后传热系数”20th Int。
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H. Mori: "Dryout Quality and Post-Dryout Heat Transfer Coefficient for a Refrigerant Flowing in Horizontal Evaporator Tubes"20th Int. Congress of Refrigeration. (印刷中). (2000)
H. Mori:“水平蒸发器管中制冷剂的干燥质量和干燥后传热系数”第 20 届国际制冷大会(2000 年出版)。
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K.YOSHIDA: "Convective Heat Transfer Enhancement of a Rotating Drum for the Permanent Magnet Type Eddy Current Retarder"Proc. of 1999 National Heat Transfer Conference, ASME. NHTC99-115. 1-6 (1999)
K.YOSHIDA:“用于永磁型涡流减速器的旋转滚筒的对流传热增强”Proc。
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H.Mori: "Dryout Quality and Post-Dryout Heat Transfer Coefficient for a Refrigerant Flowing in Horizontal Evaporator Tubes"Proc. of the 20th Int. Congress of Refrigeration. (印刷中). (2000)
H.Mori:“水平蒸发器管中制冷剂的干燥质量和干燥后传热系数”,第 20 届国际制冷大会论文集(2000 年)。
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森 英夫: "管内流れにおける限界熱流束" 日本機械学会75期通常総会講演会資料集. 4. 518-519 (1998)
Hideo Mori:日本机械工程师学会第 75 届普通大会的“管流中的临界热通量”材料。4. 518-519 (1998)
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