| 换热设备螺旋和直细通道内扇形凹穴对流体流动和传热的影响 |
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| 引用本文： | 冯振飞,朱礼,林清宇,李欢,刘鹏辉,胡华宇,杨 梅,黄祖强.换热设备螺旋和直细通道内扇形凹穴对流体流动和传热的影响[J].农业工程学报,2017,33(11):254-261. |
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| 作者姓名： | 冯振飞 朱礼 林清宇 李欢 刘鹏辉 胡华宇 杨 梅 黄祖强 |
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| 作者单位： | 1. 广西大学化学化工学院,南宁,530004;广西大学广西石化资源加工及过程强化技术重点实验室,南宁,530004;华南理工大学机械与汽车工程学院,广州,510641;2. 广西大学化学化工学院,南宁,530004;3. 广西大学化学化工学院,南宁,530004;广西大学广西石化资源加工及过程强化技术重点实验室,南宁,530004 |
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| 基金项目： | 国家自然科学基金 (51463003)；广西自然科学基金 (2014GXNSFBA118051，2016GXNSFAA380210，2016GXNSFAA380217)；广西石化资源加工及过程强化技术重点实验室主任基金(2015Z012)；南宁市科技攻关项目(20155345) |
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| 摘 要： | 为探究结构表面(如凹穴)对换热设备螺旋和直细通道内流体流动和传热影响的差异,在这2种通道的两侧面加入扇形凹穴,并采用数值方法研究其在不同雷诺数下流动、传热、熵产以及综合性能的影响。结果表明:凹穴对螺旋细通道内流体的流动影响明显,摩阻系数最大提高23%,而对传热和综合性能几乎没有影响;低雷诺数时凹穴对直细通道内流体的流动、传热和综合性能的影响不明显,而高雷诺数时影响显著,摩阻系数和努塞尔数最大分别提高50%和45%,最大传热强化因子达1.27;凹穴可减少螺旋和直细通道内流体流动和传热过程的熵产,但在高雷诺数时才比较明显地减少,且对直细通道的影响大于螺旋细通道,熵产增大数的最小值分别为0.34和0.73。研究结果可为微细通道换热设备的性能改善提供参考。
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| 关 键 词： | 传热 换热设备 流体 细通道 凹穴 熵产率 数值模拟 |
| 收稿时间： | 2016/11/10 0:00:00 |
| 修稿时间： | 2017/5/15 0:00:00 |
Effects of fan cavities on fluid flow and heat transfer in helical and straight mini-channels of heat exchanger |
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| Feng Zhenfei,Zhu Li,Lin Qingyu,Li Huan,Liu Penghui,Hu Huayu,Yang Mei and Huang Zuqiang.Effects of fan cavities on fluid flow and heat transfer in helical and straight mini-channels of heat exchanger[J].Transactions of the Chinese Society of Agricultural Engineering,2017,33(11):254-261. |
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| Authors: | Feng Zhenfei Zhu Li Lin Qingyu Li Huan Liu Penghui Hu Huayu Yang Mei and Huang Zuqiang |
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| Institution: | 1. School of Chemistry and Chemical Engineering, Guangxi University, Nanning 530004, China; 2. Guangxi Key Laboratory of Petrochemical Resource Processing and Process Intensification Technology, Guangxi University, Nanning 530004, China; 3. School of Mechanical and Automotive Engineering, South China University of Technology, Guangzhou 510641, China;,1. School of Chemistry and Chemical Engineering, Guangxi University, Nanning 530004, China;,1. School of Chemistry and Chemical Engineering, Guangxi University, Nanning 530004, China; 2. Guangxi Key Laboratory of Petrochemical Resource Processing and Process Intensification Technology, Guangxi University, Nanning 530004, China;,1. School of Chemistry and Chemical Engineering, Guangxi University, Nanning 530004, China;,1. School of Chemistry and Chemical Engineering, Guangxi University, Nanning 530004, China;,1. School of Chemistry and Chemical Engineering, Guangxi University, Nanning 530004, China;,1. School of Chemistry and Chemical Engineering, Guangxi University, Nanning 530004, China; and 1. School of Chemistry and Chemical Engineering, Guangxi University, Nanning 530004, China; |
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| Abstract: | Abstract: With the rapid development of microminiaturization technology and the urgent requirements of industrial field, the sizes of many devices are reduced continually. This causes the thermal load to increase sharply when the device is working, and further leads to the decreasing of the working stability gradually. So the conventional heat exchanger can''t meet the heat transfer requirement for these micro-devices. Thus, the micro/mini-channel heat exchanger emerges as the times require. This exchanger has many advantages, such as compact structure, high efficiency for heat dissipation, low power consumption and few coolant requirements. These advantages motivate many researchers to conduct numerous studies on the micro/mini-channel heat exchanger continuously to further enhance heat transfer performance. Adding cavities, fins or ribs on the wall of the channel is a solution for enhancing heat transfer performance in the micro/mini-channel heat exchanger. As we know, the helical and straight channels are widely applied to the heat exchanger. The difference between both channels is the existence of secondary flow in former, inducing heat transfer enhancement. Therefore, it is important to understand the effects of cavities or fins on the fluid flow and heat transfer enhancement in the helical and straight micro/mini-channel heat exchangers. As a consequence, the cavities are added on the both sidewalls of helical and straight mini-channels in this work, and the effects of the cavities on the fluid flow and heat transfer in the helical and straight mini-channels are studied using numerical simulation method. Specifically, the comparative analysis in the effects of cavities on the flow, heat transfer, entropy generation and overall performance in the helical and straight mini-channels is performed based on the first and second thermodynamics law. This aims to analyze the different effects of cavities on both mini-channels. The cross-sections for both mini-channels are the same, and the width and height of this cross-section are 3 and 3 mm, respectively. The working conditions include the Reynolds number of 168-2017, the heat flux density of 1.145 98×105 and 1×105 W/m2 for helical and straight mini-channels, respectively, based on the condition of different heating area and same power input. The numerical results show that for helical mini-channel, the cavities can increase flow resistance, and the maximum increasement reaches up to 23%. But they have no obvious influence on heat transfer performance. For straight mini-channel, the cavities can slightly reduce flow resistance and heat transfer performance when the Reynolds number is less than 1008. However, they rapidly increase flow resistance and heat transfer performance when the Reynolds number is greater than 1008, and the friction factor and Nusselt number grow to 50% and 45% respectively. In the whole Reynolds number range, the cavities can''t improve the overall performance in the helical mini-channel. Although the cavities slightly weaken the overall performance in the straight mini-channel at low Reynolds number, they obviously enhance the overall performance at high Reynolds number, and the maximum thermal enhancement factor grows to 1.27. The results of entropy generation analysis indicate that the cavities can reduce irreversible loss in the flow and heat transfer process for helical and straight mini-channels, thereby improving effective utilization of thermal energy. However, the decrement rate of irreversible loss for straight mini-channel with the cavities is greater than that for helical mini-channel, for the former''s decrement rate is about 2 times that of the latter. This work provides a reference for improving the performance of heat exchanger with mini/micro-channels. |
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| Keywords: | heat transfer heat exchanger fluids mini-channel cavity entropy generation numerical simulation |
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