冲击双层壁内通道表面换热系数的研究

为了研究双层壁内通道表面换热情况和冲击距离对换热影响,对双层壁结构内通道上、下表面的换热系数进行实验测量。由获得的换热系数来分析研究双层壁内部换热。并对冲击射流的机理作了分析。研究结果表明,在双层壁结构中,在高雷诺数时,在冲击板表面上会出现两个峰值;在进气板表面上也会出现位置随冲击高度变化的一高换热区;层板内通道表面上的换热系数随冲击距离的减小而增大。     

浮升力对双旋转轴间流动换热影响的数值模拟

利用Boussinesq假设，采用混合长度模型，对具有轴向通流的双旋转轴间的流动换热进行了数值研究，得到了轴间气体充分发展段的速度分布、温度分布和加热边的对流换热系数，其结果在实验模型参数范围内与PfitzerH的实验研究符合较好。在此基础上，进一步数值模拟研究了同向等速旋转双轴间不可压流的离心浮升力对流动换热的影响，结果表明：离心浮升力对流动换热的影响取决于浮升力与惯性力之比GrB/Rex^2。当GrB/Rex^2≥24时，浮升力的影响十分显著，不可忽略。     

考虑气体扩散渗透的隔热材料瞬态隔热性能数值模拟

高超声速飞行器机动飞行时环境压力变化导致隔热材料沿厚度方向存在压力梯度,进而引起隔
热材料内气体的扩散渗透,影响隔热材料隔热性能。为研究气体扩散渗透对隔热材料隔热性能的影响,建立了
隔热材料内气体扩散渗透模型,采用罗斯兰德近似、有限体积法建立了隔热材料内扩散渗透及辐射导热传热计
算模型,对气体扩散渗透条件下的瞬态隔热性能进行了数值模拟。算例模拟结果表明:对2 cm 厚纳米隔热材
料,在外界气压为0. 1 MPa,绝热面为真空的状况下,当渗透率大于10-14 m2 时,气体扩散渗透开始影响隔热材
料内传热,导致隔热性能降低,气体黏性系数对气体扩散渗透有显著影响,随着黏性系数降低,气体扩散渗流现
象显著;衰减系数对绝热面温度响应有显著影响,随着衰减系数增大,绝热面温度响应显著降低。     

飞机整机线缆自动化集成检测技术研究现状和发展

飞机整机线缆集成检测是飞机总装过程中的一项重要工作,是关乎线缆制造质量高低的一个关键环节,在航空制造企业受到了广泛重视.对飞机整机线缆检测方法进行了比较和分析,介绍了线缆自动化集成检测的内涵和主要研究内容,对比分析了国内外线缆自动化集成检测的研究现状,分析和指出了线缆自动化集成检测存在的问题以及发展趋势.最后对数字孪生...     

Preliminary study on heat flux measurement data of TT-0 flight test

With the explosive development of aerospace science, the design of the new generation airliner at higher speeds is attracting more attentions. To achieve this goal, it is necessary to achieve accurate prediction of the aerodynamic heating / force loads and successful reduction of drag and heat flux. As a remedy for the existing studies which are based upon the CFD and wind tunnel tests, this study presents a flight test for the drag and heat reduction spike technology. The principal goals of this flight test were to provide reference for verifying the accuracy of the prediction technology on ground and promote the development of the drag and heat reduction technology. By adopting the OS-X rocket, the TT-0 test vehicle designed by Shenyang Aircraft Design & Research Institute reached a maximum Mach number of 5.8 and a maximum altitude of 38 km. Hypersonic and supersonic pressure data by pressure scanning valves and heat fluxes by gauges at different locations were obtained successfully. Also, heat fluxes obtained by in-house CFD code are illustrated in comparison with the flight data. The results indicate that the numerical errors are large in most cases. More technologies, such as more CFD codes and more numerical procedures, should be adopted to conduct studies on this issue in the future.     

基于传热反问题方法的N_2O/C_2H_4预混推进剂燃烧室热流测量研究

测量液体火箭发动机的热载荷是获取燃烧室内部信息的重要方法。为了获取N_2O/C_2H_4预混推进剂燃烧室内壁的热载荷,建立了液体火箭发动机的热流计算的反问题方法,该方法基于对燃烧室壁面温度场的直接求解,通过对轴向多个位置测量温度的反演计算得到燃烧室内壁热流和温度。研究表明:应用文中建立的传热反问题方法能够较为准确地获得热流随时间及空间的分布;热电偶的位置对计算准确性有明显的影响,与理论深度偏差在0.2mm以内的随机深度偏差可导致超过4%热流反演误差;N_2O/C_2H_4预混推进剂燃烧室热流及温度沿轴向逐渐降低,表明燃烧室内的反应释热过程主要在燃烧室头部附近发生。     

新型翅片式减涡器减阻特性数值研究

为了降低压气机径向引气过程中的压力损失,在设计出新型翅片单元结构的基础上,研究了新型翅片单元结构对径向引气压力损失的影响规律,对不同转速、新型翅片结构的去旋系统开展了数值研究,得到了不同工况下压气机共转盘腔径向引气的流场结构及压力损失分布曲线。研究结构表明:新型翅片单元结构能够抑制盘腔内气流旋流比,降低引气压力损失;翅片单元通道宽度和高度均存在最佳值使得减涡器减阻效果较好,在优选结构翅片单元通道宽度L=0.78,通道高度R3=0.97的条件下,其减阻效果较简单盘腔模型提高86.5%。高低翅片结构能起到较好的减阻效果,随着单侧翅片高度的升高减阻效果逐渐增强,在本文结构下增加单侧翅片高度L1=0.3时减阻效果最优,且A侧或B侧翅片增加带来的减阻效益相同。一方面,最优高低翅片结构其减阻性能相比于简单盘腔模型、典型翅片式减涡器模型以及翅片单元通道宽度L=0.78,通道高度R3=0.97的结构模型分别提高87.5%,29%,7.8%;另一方面,最优高低翅片结构能够减轻翅片单元的质量,具有较高的工程应用价值。     

下缘板孔对涡轮叶片尾缘内冷通道流动换热影响的数值研究

涡轮叶片下缘板出气孔对内冷通道的流动和换热性能有较大影响。通过数值模拟方法研究下缘板出 气孔对尾缘和下缘板双路出气涡轮叶片尾缘内冷通道内的流动和换热特性,对比分析孔径、孔形和孔位置对尾 缘溢流孔流量系数、尾缘出流比、尾缘通道内总压系数和尾缘内冷腔壁面换热特性的影响。结果表明:下缘板 出气孔孔径对流量系数分布的影响显著,孔径增大,尾缘溢流孔流量系数下降,尾缘出流比减小,尾缘内冷通道 内压力损失降低,内冷腔平均换热系数增大;孔形对上游内冷通道内流动和换热几乎没有影响;孔位置变化对 内冷通道壁面整体的换热系数影响很小,对局部影响较大。     

RTM用6818高温环氧树脂化学流变特性研究

以树脂传递模塑(RTM)用6818高温环氧树脂体系的化学流变特性研究为目的,以差示扫描量热法(DSC)和黏度实验为基础,采用外推法初步确定了6818树脂体系的固化工艺制度。依据双阿累尼乌斯方程建立了树脂体系的化学流变模型,模型曲线与实验数据的吻合性良好。模型分析表明,在80～100℃内树脂体系黏度低于200 mPa·s的时间大于12 h,可以作为6818树脂比较理想的注胶温度。该模型能够反映6818树脂黏度变化规律,预报该树脂体系的RTM工艺窗口。     

Numerical investigation on flow and heat transfer characteristics of supercritical RP-3 in inclined pipe

Numerical simulations of flow and heat transfer to supercritical RP-3 through the inclined tubes have been performed using LS k–e model embedded in Fluent. The physical properties of RP-3 were obtained using the generalized corresponding state laws based on the fourcomponent surrogate model. Mass flow rate is 0.3 g/s, system pressure is 3 MPa, inlet temperature is 373 K. Inclination of the inclined pipe varied from -90° to 90°, with heat flux varied from 300 k W/m~2 to 400 kW/m~2. Comparison between the calculated result and the experimental data indicates the range of error reasonable. The results of ±45° show that temperature inhomogeneity in inclined pipe produce the secondary flow in its cross section due to the buoyancy force. Depending on the strength of the temperature inhomogeneity, there will be two different forms of secondary flow and both contribute to the convective heat transfer in the pipe. The secondary flow intensity decreases when the inhomogeneity alleviates and thermal acceleration will play a leading role. It will have a greater impact on the turbulent flow to affect the convective heat transfer in the pipe. When changing the inclination, it affects the magnitude of the buoyant component in flow direction. The angle increases, the buoyancy component decreases. And the peak temperature of wall dominated by the secondary flow will move forward and increase in height.