Research of Boiling Heat Transfer and Flow Pattern of Refrigerant in Horizontal Small-Diameter Tubes

水平小管径管内制冷剂沸腾传热及流动规律研究

• 批准号: 13650212
• 负责人: SAITOH Shizuo
• 金额: $ 2.37万
• 依托单位: THE UNIVERSITY OF TOKYO
• 依托单位国家: 日本
• 项目类别: Grant-in-Aid for Scientific Research (C)
• 财政年份: 2001
• 资助国家: 日本
• 起止时间: 2001 至 2002
• 项目状态: 已结题
• 来源: https://kaken.nii.ac.jp/grant/KAKENHI-PROJECT-13650212/
• 关键词: Boiling heat transfer; Flow pattern; Evaporator; Refrigerator; Pressure drop; Dryout; Tube diameter; Correlation; 蒸発器

Boiling heat transfer to HFC134a and flow pattern were investigated in horizontal small-diameter tubes, 0.51 mm, 1.12 mm and 3.1mm I.D. Boiling heat transfer coefficients were obtained for mass velocity of 150 〜 400 kg/m^2s, and heat flux of 5〜30 kW/m^2. The flow patterns of plug, slug, wavy and annular flows were observed at inlet qualities ranging from zero to 0.7 for the range of mass velocity of 100〜400 kg/m^2s. For the low inlet quality and high heat flux, the oscillated refrigerant flow occurred and oscillations of wall temperature and pressure were observed in the heated tube. The boiling heat transfer coefficients were affected by the flow patterns, and were considerably reduced for the oscillated and slug flow. It was shown that the contribution of the forced convective evaporation to boiling heat transfer decreases, as the tube diameter decreases. A heat transfer deterioration model and a dryout prediction model were proposed, and predictive value and experimental value are correlated well. The pressure drop in 3.1 mm tube agreed well with the prediction by the correlation of Lockhart-Martinelli, but in the case of the tube diameter 0.51 mm, it agreed well by the homogenous model.

在水平小直径管（0.51 mm、1.12 mm 和 3.1mm I.D.）中研究了 HFC134a 的沸腾传热和流型，获得了质量速度为 150 〜 400 kg/m^2s、热通量为 5 时的沸腾传热系数。在入口处观察到~30 kW/m^2 的流型：塞流、段塞流、波状流和环形流。在质量速度为 100〜400 kg/m^2s 的范围内，质量从 0 到 0.7 对于低入口质量和高热通量，在加热管中出现了振荡制冷剂流动并且观察到壁温和压力的振荡。沸腾传热系数受到流动模式的影响，并且对于振荡流和段塞流而言，沸腾传热系数显着降低。随着管径的减小，沸腾传热减小，提出了传热恶化模型和干涸预测模型，预测值和实验值相关性良好，3.1 mm 管内的压降与相关性预测吻合良好。 Lockhart-Martinelli 的模型，但在管直径为 0.51 mm 的情况下，与齐次模型非常吻合。

项目成果

Shizuo Saitoh, Hirofumi Daiguji and Eiji Hihara: "Boiling Heat Transfer and Flow Pattern of Refrigerant inside a Horizontal Tubes"38^<th> National Heat Transfer Symposium of Japan. 5. 897-898 (2001)

Shizuo Saitoh、Hirofumi Daiguji 和 Eiji Hihara：“水平管内制冷剂的沸腾传热和流动模式”第 38 届日本全国传热研讨会。

斎藤 静雄: "冷媒HFC134aの水平細管内の沸騰熱伝達と圧力損失"第39回日本伝熱シンポジュウム講演論文集. (発表予定). (2002)

Shizuo Saito：“制冷剂 HFC134a 水平管中的沸腾传热和压力损失”第 39 届日本传热研讨会论文集（预定演讲）。

Shizuo Saitoh, Hirofumi Daiguji and Eiji Hihara: "Boiling Heat Transfer and Pressure Drop of HFC134a in Horizontal Small-Diameter Tubes"39^<th> National Heat Transfer Symposium of Japan. 3. 667-668 (2002)

Shizuo Saitoh、Hirofumi Daiguji 和 Eiji Hihara：“水平小直径管中 HFC134a 的沸腾传热和压降”第 39 届日本全国传热研讨会。

斎藤 静雄: "水平管内沸騰熱伝達における管径の影響-諸因子(熱流束、質量流束等)の局所熱伝達率への影響-"第37回空気調和・冷凍連合講演会講演論文集. 121-124 (2003)

Shizuo Saito：《管径对水平管道沸腾传热的影响——各种因素（热通量、质量通量等）对局部传热系数的影响——》第37届空调制冷联盟会议论文集121-。 124（2003）

斎藤 静雄: "水平管内沸騰熱伝達における管径の影響 ?諸因子(熱流束、質量流束等)の局所熱伝達率への影響?"第37回空気調和・冷凍連合講演会講演論文集. (発表予定). (2003)

Shizuo Saito：“管道直径对水平管道沸腾传热的影响？各种因素（热通量、质量通量等）对局部传热系数的影响？”第37届空调制冷联盟会议论文集。预定）（2003）。