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首页> 外文期刊>Journal of Mechanical Science and Technology >Heat transfer characteristics and entropy generation for wing-shaped-tubes with longitudinal external fins in cross-flow
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Heat transfer characteristics and entropy generation for wing-shaped-tubes with longitudinal external fins in cross-flow

机译:带有纵向外部翅片的横流翅形管的传热特性和熵产生

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A numerical study is conducted to clarify heat transfer characteristics, effectiveness and entropy generation for a bundle of wingshaped-tubes attached to Longitudinal fins (LF) at downstream side. The air-side Rea ranged from 1.8 x 10(3) to 9.7 x 10(3). The fin height (h(f)) and fin thickness (delta) have been changed as: (2 mm a parts per thousand currency sign h(f) a parts per thousand currency sign 12 mm) and (1.5 mm a parts per thousand currency sign delta a parts per thousand currency sign 3.5 mm). The analysis of entropy generation is based on the principle of minimizing the rate of total entropy generation that includes the generation of entropy due to heat transfer and friction losses. The temperature field around the wing-shaped-tubes with (LF) is predicted using commercial CFD FLUENT 6.3.26 software package. Correlations of Nu(a), St(a), and Bejan number (Be), as well as the irreversibility distribution ratio (I broken vertical bar) in terms of Re-a and design parameters for the studied bundle are presented. Results indicated that, installing fins with heights from 2 to 12 mm results in an increase in Nua from 11 to 36% comparing with that of wing-shaped tubes without fins (NOF). The highest and lowest values of effectiveness (epsilon) at every value of the considered Re-a range are occurred at h(f) = 6 mm and (NOF), respectively. The wing-shaped-tubes heat exchanger with h(f) = 6 mm has the highest values of (epsilon), efficiency index (eta) and area goodness factor (G (a)) and also the lowest values of I broken vertical bar and hence the best performance comparing with other arrangements. The minimum values of I broken vertical bar are occurred at h(f) = 6 mm. (Be) decreases with increasing Re-a for all studied h(f). The heat transfer irreversibility predominates for (1800 a parts per thousand currency sign Re-a a parts per thousand currency sign 4200) while the opposite is true for (6950 < Re-a a parts per thousand currency sign 9700). delta has negligible effect on Nu(a) and heat transfer irreversibility. Comparisons between the experimental and numerical results of the present study and those, previously, obtained for similar available studies showed good agreements.
机译:进行了数值研究,以弄清在下游侧附接到纵向鳍片(LF)上的一束翼形管的传热特性,有效性和熵的产生。空气侧Rea的范围从1.8 x 10(3)到9.7 x 10(3)。散热片高度(h(f))和散热片厚度(delta)已更改为:(每2毫米千分之几h(f)每12毫米千分之几)和(1.5千每千分之几货币符号delta千分之一(3.5毫米)。熵产生的分析基于最小化总熵产生速率的原理,该总熵产生速率包括由于传热和摩擦损失而产生的熵。使用商用CFD FLUENT 6.3.26软件包预测带有(LF)的翼形管周围的温度场。给出了Nu(a),St(a)和Bejan数(Be)的相关性,以及不可逆分布比(I折断的竖线)的Re-a和设计参数的相关性。结果表明,与没有翅片的翼形管相比,安装高度为2到12 mm的翅片会使Nua从11%增至36%。在所考虑的Re-a范围的每个值处,有效性(ε)的最高和最低值分别出现在h(f)= 6 mm和(NOF)处。 h(f)= 6 mm的翼形管式换热器具有最高的ε,效率指数(η)和面积优度因子(G(a)),并且具有最低的I折断竖线值因此,与其他安排相比,其表现最佳。垂直折线I的最小值出现在h(f)= 6 mm处。对于所有研究的h(f),(Be)随Re-a的增加而减小。传热不可逆性占主导地位(1800千分之一货币符号Re-a一千分之一货币符号4200),而相反则适用(6950

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