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TRANSIENT HEAT CONDUCTION DURING QUENCHING OF DOWNWARD FACING COPPER AND STAINLESS STEEL CONVEX SURFACES

 

作者: MohamedS. El-Genk,   Cheng Gao,  

 

期刊: Numerical Heat Transfer, Part A: Applications  (Taylor Available online 1996)
卷期: Volume 29, issue 6  

页码: 543-573

 

ISSN:1040-7782

 

年代: 1996

 

DOI:10.1080/10407789608913806

 

出版商: Taylor & Francis Group

 

数据来源: Taylor

 

摘要:

Quenching experiments were performed to determine the effect of watt material properties on pool boiling heat transfer for downward facing convex surfaces( radius of curvature 218.5 mm) in saturated water. Experiments employed 303e-type stainless steel and copper test sections having identical dimensions ( 75 mm in diameter and 20 mm thick). Pool boiling curves were constructed on the basis of two-dimensional numerical solution of transient heat conduction in spherical coordinates( r, 9) in test sections during quenching. The measured temperature histories at nine interior locations near the boiling surface ( ∼0.5 mm) provided a time-dependent boundary condition for the numerical solution. To ensure stability and reduce both computer storage and execution time, the numerical solution used the alternating direction implicit ( ADD method with control volume representations. A sensitivity analysis was conducted to assess the effect of grid size on computation time as well as the accuracy of calculated temperatures and pool boiling heat flux values. Best results were obtained using a 20 × 20 network of control volumes and a noniterative approach, whereas the computation time on a Pentium 90-MHz PC for the entire pool boiling curve was about 7% of real time. Calculated temperatures near the top surface ( ∼5 mm) agreed with measured values to within 0.5 and 2.5 K for copper and stainless steel, respectively. The error in the overall energy balance in the test section, performed after each time interval, was less than 0.001%. The thermal diffusivity of test section material strongly affected both radial conduction within the section and lateral conduction near the boiling surface and, hence, the local pool boiling curves as well as the maximum and minimum pool boiling heat flux values.

 

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