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Numerical Study of N-Decane Convective Heat Transfer with Endothermic Pyrolytic Reaction under a Constant Wall Temperature and Supercritical Pressures

机译:恒定壁温和超临界压力下具有吸热热解反应的正癸烷对流换热的数值研究

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A numerical study was conducted on the turbulent convective heat transfer of n-decane in a mini tube with endothermic pyrolytic reaction under a constant wall temperature and supercritical pressures. A onestep pyrolytic reaction mechanism of n-decane was employed. Numerical results with and without pyrolysis were compared and discussed. Effects of the inlet velocity and pressure on heat transfer processes were investigated. It is found that the wall heat flux at the thermal exit can be increased by more than 280% due to the pyrolytic reaction under certain operation conditions. Furthermore, the flow velocity increases significantly as n-decane is thermally decomposed to low-molecular-weight components. Heat absorption from the endothermic pyrolytic reaction dictates the convective heat transfer process in the high temperature region toward the thermal exit. This effect weakens as the inlet velocity increases. The pressure effect on heat absorption from pyrolysis is quite weak under the tested operation conditions.
机译:在恒定管壁温度和超临界压力下,在具有吸热热解反应的微型管中,对正癸烷的湍流对流换热进行了数值研究。采用正癸烷的一步热解反应机理。比较和讨论了有和没有热解的数值结果。研究了入口速度和压力对传热过程的影响。已经发现,由于在某些操作条件下的热解反应,热出口处的壁热通量可以增加280%以上。此外,当正癸烷热分解为低分子量组分时,流速显着增加。吸热热解反应吸收的热量决定了对流传热过程在高温区域朝着热出口。随着进口速度的增加,这种影响减弱。在测试的操作条件下,热解吸收热量的压力作用非常弱。

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