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摘要:
壁面质量引射可有效降低壁面热流和摩擦阻力,是解决高超声速飞行器热防护问题的备选方案之一。选取二维钝楔为计算模型,展开质量引射对降热减阻的数值模拟研究,对比分析了3种不同工质引射气体(热解气体、水蒸气和二氧化碳)对气动力热特性的影响。将热流分解为对流热流和扩散热流可知,热解气体引射降低了对流热流和扩散热流;而水蒸气和二氧化碳引射虽然降低了对流热流,但增大了扩散热流,且水蒸气增大扩散热流的效果更明显,使得总热流增加。此外,3种不同工质引射气体均通过降低壁面附近的速度梯度来降低壁面的摩擦阻力,其中,热解气体引射降低的速度梯度最大,减阻效果最好。
Abstract:One way to address the thermal protection issue of hypersonic vehicles is through wall mass injection, which can successfully lower skin friction and wall heat flow. The effects of three distinct gases (pyrolysis gas, water vapor, and carbon dioxide) on aerodynamic force and thermal characteristics are compared and analyzed, and the numerical simulation of mass injection on the heat flux and skin friction of the wall is investigated using a two-dimensional blunt wedge as the calculation model. It is possible to determine that the pyrolysis gas injection lowers the convective and diffusion heat flux by splitting the heat flux into these two categories. Both carbon dioxide injection and water vapor enhance the diffusion heat flux while decreasing the convective heat flow. The effect of water vapor raising the diffusion heat flux is more noticeable, leading to an increase in the overall heat flux. Additionally, by lowering the velocity gradient close to the wall, all three gases can lessen the skin-friction of the wall, with pyrolysis gas injection having a greater impact.
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表 1 引射工质质量分数
Table 1. Mass injection conditions
引射工质 质量分数/% H2O 3.08 CO2 1.22 N2 67.80 H2 0.72 O2 2.44 CO 12.50 OH 3.71 NO 2.08 N 0.0078 O 6.46 表 2 来流工况
Table 2. Flow condition
速度/(m·s−1) 来流密度/(kg·m−3) 温度/K 迎角/(°) 7349 1.6×10−4 233 9.5 表 3 质量引射工质
Table 3. Mass injection conditions
引射工质 各组分占比 H2O H2 CH4 CO CO2 水蒸气 1 0 0 0 0 二氧化碳 0 0 0 0 1 热解气体 0.66 0.23 0.06 0.01 0.01 表 4 引射气体摩尔质量
Table 4. Molar mass of injection gas
g/mol 热解气体 水蒸气 二氧化碳 14.04 18.02 44.01 表 5 引射气体各组分扩散系数和焓值
Table 5. Diffusion coefficient and enthalpy of each component of injection gas
引射工质 组分 扩散系数Ds/
(m2·s−1)焓值$h_{s}^{a} $/
(MJ·kg−1)$ \displaystyle\sum\limits_{s=1}^{ns}{D}_{s}h_{s}^{a}\dfrac{\partial {Y}_{s}}{\partial n}\Big/ $
((m2·MJ)·(s·kg)−1)热解气体 H2O 0.25 −10.75 21.17 H2 0.28 18.02 CH4 0.14 0.35 CO 0.16 −2.56 CO2 0.13 −7.54 水蒸气 H2O 0.25 −10.75 133.54 二氧化碳 CO2 0.13 −7.54 42.38 -
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