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首页> 外文期刊>Mathematical Problems in Engineering: Theory, Methods and Applications >Computational Fluid Dynamics Analysis of Flow Patterns, Pressure Drop, and Heat Transfer Coefficient in Staggered and Inline Shell-Tube Heat Exchangers
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Computational Fluid Dynamics Analysis of Flow Patterns, Pressure Drop, and Heat Transfer Coefficient in Staggered and Inline Shell-Tube Heat Exchangers

机译:交错与内联壳管热交换器流动模式,压降和传热系数的计算流体动力学分析

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In this numerical study, the heat transfer performance of shell-and-tube heat exchangers (STHXs) has been compared for two different tube arrangements. STHX having 21 and 24 tubes arranged in the inline and staggered grid has been considered for heat transfer analysis. Shell-and-tube heat exchanger with staggered grid arrangement has been observed to provide lesser thermal stratification as compared to the inline arrangement. Further, the study of variation in the mass flow rate of shell-side fluid having constant tube-side flow rate has been conducted for staggered grid structure STHX. The mass flow rate for the shell side has been varied from 0.1?kg/s to 0.5?kg/s, respectively, keeping the tube-side mass flow rate as constant at 0.25?kg/s. The influence of bulk mass-influx transfer rate on heat transfer efficiency, effectiveness, and pressure drop of shell-tube heat exchangers has been analyzed. CFD results were compared with analytical solutions, and it shows a good agreement between them. It has been observed that pressure drop is minimum for the flow rate of 0.1?kg/s, and outlet temperatures at the shell side and tube side have been predicted to be 40.94°C and 63.63°C, respectively.
机译:在该数值研究中,已经将壳管热交换器(STHXS)的传热性能进行了比较了两种不同的管布置。 STHX具有布置在线和交错电网中的21和24个管,用于传热分析。已经观察到具有交错栅格布置的壳管热交换器,以提供与内联排列相比的较小的热分层。此外,已经对具有恒定管侧流速的壳侧流体的质量流量的变化的研究进行了用于交错的网格结构STHX。壳侧的质量流量分别从0.1Ωkg / s变化至0.5Ωkg / s,使管侧质量流量保持在0.25Ωkg / s的恒定。分析了散装质量流量转移率对壳管热交换器的传热效率,有效性和压降的影响。将CFD结果与分析解决方案进行比较,并显示它们之间的良好一致性。已经观察到,对于0.1Ω·kg / s的流速,压降是最小的,并且壳侧和管侧的出口温度分别预测为40.94°C和63.63°C。

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