Development Of A New Heat Transfer Correlation For Flow Of Supercritical Steam In Spiral Tubes Under Deteriorated Heat Transfer Regime

IF 2.8 4区 工程技术 Q2 ENGINEERING, MECHANICAL
D. Kanungo
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引用次数: 0

Abstract

Heat transfer to supercritical steam flowing inside spiral tube under deteriorated heat transfer regime is investigated in this work using three-dimensional numerical simulations. The numerical solver is first validated with experimental results and subsequently multiple simulation cases are formulated with spiral tube by varying the flow and thermal conditions. The wall temperature and heat transfer co-efficient of spiral tubes are compared with the same of straight tubes. Over the parameters range considered, the heat transfer co-efficient is improved by 88% when straight tube is replaced with spiral tube, for similar flow and thermal conditions. Most significantly, the deteriorated heat transfer regime, which is otherwise witnessed in straight tubes is completely avoided by using spiral tubes, for the similar flow conditions. Tangential velocity, which arise due to centrifugal force is the primary reason of enhanced heat transfer in spiral tubes. Three standard heat transfer co-relations are tested for spiral geometry under deteriorated heat transfer regime and it is found that none of those can predict the heat transfer co-efficient accurately. Using the simulation results along with Buckingham p-theorem, a new co-relation for heat transfer co-efficient is proposed for spiral tubes carrying supercritical steam and operating under deteriorated heat transfer regime. The new co-relation can predict the wall temperature and heat transfer co-efficient accurately. The co-relation has an error band of +/-25%.
变质传热条件下螺旋管内超临界蒸汽流动传热关系式的建立
本文采用三维数值模拟的方法,研究了变质传热条件下螺旋管内超临界蒸汽的换热问题。首先用实验结果验证了数值解的正确性,然后通过不同的流动和热条件,建立了螺旋管的多个模拟案例。对螺旋管与直管的壁温和传热系数进行了比较。在考虑的参数范围内,在相同的流动和热条件下,用螺旋管代替直管的换热系数提高了88%。最重要的是,在类似的流动条件下,使用螺旋管完全避免了在直管中出现的传热恶化现象。由于离心力而产生的切向速度是螺旋管内传热增强的主要原因。对螺旋几何在变传热工况下的三种标准换热相关关系进行了测试,发现没有一种标准换热相关关系能准确地预测换热系数。利用模拟结果,结合Buckingham p-定理,提出了在变质传热工况下承载超临界蒸汽的螺旋管传热系数的新关系式。该关系式可以准确地预测壁面温度和传热系数。相关关系的误差范围为+/-25%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
自引率
0.00%
发文量
182
审稿时长
4.7 months
期刊介绍: Topical areas including, but not limited to: Biological heat and mass transfer; Combustion and reactive flows; Conduction; Electronic and photonic cooling; Evaporation, boiling, and condensation; Experimental techniques; Forced convection; Heat exchanger fundamentals; Heat transfer enhancement; Combined heat and mass transfer; Heat transfer in manufacturing; Jets, wakes, and impingement cooling; Melting and solidification; Microscale and nanoscale heat and mass transfer; Natural and mixed convection; Porous media; Radiative heat transfer; Thermal systems; Two-phase flow and heat transfer. Such topical areas may be seen in: Aerospace; The environment; Gas turbines; Biotechnology; Electronic and photonic processes and equipment; Energy systems, Fire and combustion, heat pipes, manufacturing and materials processing, low temperature and arctic region heat transfer; Refrigeration and air conditioning; Homeland security systems; Multi-phase processes; Microscale and nanoscale devices and processes.
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