超临界n -十二烷在热裂加热圆管内流动的数值研究

Shuto Yatsuyanagi, Takashi Furusawa, S. Yamamoto, Takuo Onodera, S. Tomioka
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摘要

采用求解可压缩Navier-Stokes方程的数值预处理方法,对正十二烷(C12H26)在含热裂纹的加热圆管内的流动进行了数值模拟。用Cantera法测定了正十二烷热裂解反应速率常数。用亥姆霍兹自由能状态方程计算了纯正十二烷及其分解组分的热物理性质。出口温度与实验结果吻合较好,最大误差为3.2%。出口温度随壁面温度的升高而升高,壁面温度较高时,出口温度的升高幅度略小。从径向热扩散系数的角度讨论了壁面温度条件与传热之间的关系。我们还比较了正辛烷(C8H18)的径向分布,包括温度、热扩散率和未反应的碳氢化合物的质量分数。热裂主要发生在受热壁附近的高温区域。分解组分的密度远低于正十二烷和正辛烷的密度,导致混合物在加热壁附近的密度显著降低。分解组分的热物性变化影响了超临界油气流动。在正十二烷和正辛烷流动中,由分解组分和湍流引起的热扩散率影响温度分布和质量分数。最后,我们比较了正十二烷和正辛烷的出口转化率。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Numerical Investigation of Supercritical N-Dodecane Flows in a Heated Circular Pipe With Thermal Cracking
Supercritical n-dodecane (C12H26) flows in heated circular pipes with thermal cracking were numerically investigated using a numerical preconditioning method for solving the compressible Navier–Stokes equations. The reaction rate constants for thermal cracking of n-dodecane were determined using Cantera. The thermophysical properties of pure n-dodecane and its decomposed components were calculated using the Helmholtz free-energy equation of state. The outlet temperatures agreed well with experimental results, and the maximum error was 3.2%. The outlet temperature increased with the wall temperature condition, although the rate of increase became slightly smaller when the wall temperature was high. We discussed the relationship between the wall temperature condition and heat transfer in terms of thermal diffusivity in the radial direction. We also compared the radial distributions with those of n-octane (C8H18) in terms of temperature, thermal diffusivity, and mass fraction of unreacted fed hydrocarbons. Thermal cracking mainly occurred in a high-temperature region near the heated wall. The density of the decomposed components was much lower than that of n-dodecane and n-octane, resulting in a significant decrease in the mixture’s density near the heating wall. The decomposed components affected the supercritical hydrocarbon flows owing to changes in their thermophysical properties. The thermal diffusivity due to the decomposed components and turbulence affects the temperature distributions and mass fraction in n-dodecane and n-octane flows. Finally, we compared the outlet conversion rates of n-dodecane and n-octane flows.
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