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Experimental investigation of heat transfer and second law analysis in a pebble bed channel with internal heat generation

机译:卵石床内部传热的传热实验及第二定律分析

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This paper studies experimentally the forced convection heat transfer of turbulent flow in a cylindrical pebble bed channel with internal heat generation. Exergy and entropy generation analyses are performed to optimize energy conversion in the system identify the destruction of exergy in the pebble bed channel. Stainless steel spheres are used in stacked pebble bed channel. Internal heating is generated uniformly by electromagnetic induction heating method in metallic spheres. Dry air is used as the working fluid in the process of cooling of the heated spheres. The experiment is performed for turbulent flow regimes with Reynolds (Re_d) number (based on the diameter of the spheres) in the range of 920-2570, which is equal to Reynolds (Re) number, based on channel diameter, in the range of 4500-10,000. The effects of different parameters, including spheres diameter (d = 5.5, 6.5 and 7.5 mm), inlet volumetric flow rate (V̇) and internal heat generation (Q) on the forced convection heat transfer, exergy transfer and entropy generation are studied. For second law and exergy analyses, mean exergy transfer Nusselt number (Nu_e) and entropy generation number (N_s) are investigated. Results show that for a fixed d and Q, the mean exergy transfer Nusselt number (Nu_e) decreases with the increase of Re_d number until it becomes zero for a critical Re_d number. This critical Re_d number found to be about 1450, 1800 and 2300 for d = 5.5, 6.5 and 7.5 mm, respectively. Further increase in the Re_d number, decreases Nu_e to negative values. It is found for spheres with diameter of d = 5.5 mm and for a fixed Q, as Re_d increases, the entropy generation number N_s increases monotonically. While, for d > 5.5 mm and fixed Q, the entropy generation number (N_s) decreases with the increase of Re_d number up to a critical Re_d value that makes N_s to be minimum. Further increase in Re_d number, increases N_s. It is also found that for Re_d > 1800, among the sphere diameters studied in this work, balls with highest diameters yield the minimum entropy generation in the system.
机译:本文研究了内部产生热量的圆柱卵石床通道内湍流的强迫对流传热。进行了火用和熵生成分析,以优化系统中的能量转换,从而确定卵石床通道中的火用破坏。不锈钢球用于堆积卵石床通道。内部加热是通过电磁感应加热方法在金属球中均匀产生的。在加热球体的冷却过程中,将干燥空气用作工作流体。针对湍流态进行了实验,雷诺数(Re_d)(基于球体的直径)在920-2570的范围内,它等于雷诺数(Re)基于通道直径的数,在以下范围内4500-10,000。研究了不同参数的影响,包括球体直径(d = 5.5、6.5和7.5mm),入口体积流量(V and)和内部热量产生(Q)对强制对流热量传递,(火用)传递和熵产生的影响。对于第二定律和本能分析,研究了平均本能传递努塞尔数(Nu_e)和熵产生数(N_s)。结果表明,对于固定的d和Q,平均本能传递努塞尔数(Nu_e)随着Re_d数的增加而减小,直到对于关键Re_d数变为零。对于d = 5.5、6.5和7.5mm,此关键Re_d数分别约为1450、1800和2300。 Re_d数的进一步增加将Nu_e减小为负值。对于直径为d = 5.5mm的球体,对于固定的Q,发现随着Re_d的增加,熵产生数N_s单调增加。而对于d> 5.5mm且固定Q值,熵生成数(N_s)随Re_d数的增加而减小,直至使N_s最小的临界Re_d值。 Re_d数进一步增加,N_s增加。还发现,对于Re_d> 1800,在这项工作研究的球直径中,直径最大的球在系统中产生的熵最小。

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