Study on advantages of flow resistance reduction for honeycomb-like double-wall cooling structures
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摘要:
高冷效涡轮叶片需要采用双层壁冷却结构,但已有大量研究表明其冷气流动阻力过大,导致该类结构应用困难。为改善这一问题,一种蜂巢式双层壁冷却结构已经被提出。基于自研的小型风洞实验系统和3D打印制备的实验件,在常温常压工况下对两种双层壁结构进行了流阻对比实验。结果表明在相同的结构准则参数和来流雷诺数下,蜂巢式结构的总压损失比典型层板减少了20.5%~22.5%,总压恢复系数提高了最多1.4%;同时对实验过程进行了仿真复现,进一步明晰了该结构可有效组织气流和抑制多类旋涡的减阻机理。通过对实验结果的不确定性分析,以及实验与仿真结果的相互印证,表明了所得结论的可信性。
Abstract:Double-wall cooling structure should be applied to the high-cooling efficiency turbine blade. But the previous works discovered its tremendous flow resistance, which caused the difficulties in applications. A novel honeycomb-like double-wall cooling structure was proposed to solve this issue. Flow resistance comparison experiments between 2 double-wall structures were carried out using a small wind tunnel and 3D printing components under ordinary operating conditions. Compared with the typical lamilloy with the equal structural criterion numbers, the total pressure loss of the honeycomb-like scheme could be reduced by about 20.5% to 22.5% under the same upstream Reynolds number, and the total pressure recovery coefficient could be increased by up to 1.4%. The strengthening mechanism of the novel scheme was clearly revealed by replicating numerical simulations of the experimental process, with more effective flow organization and vorticity suppression. These advantages were proved by uncertainty analysis and verification between experiment and simulation methods.
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Key words:
- turbine blade /
- honeycomb-like cooling /
- double-wall structure /
- flow resistance /
- wind tunnel test
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表 1 两模型主要结构参数
Table 1. Main structural parameters of 2 models
参数类型 参数名称 数值 有量纲 H0/mm 6.00 H4/mm 6.00 A0s/mm2 106.42 A1s/mm2 2.07 A2s/mm2 40.62 A3s/mm2 2.07 无量纲 $ \gamma $ 0.38 $ \xi $ 0.02 表 2 网格无关性验证
Table 2. Grid independence verification
网格量/万 θ/% 53 29.36 95 12.96 248 3.37 596 −1.43 表 3 湍流模型的结果相对误差θ
Table 3. Result relative deviation θ of turbulence models
% Re θ k-ε模型 k-ω模型 SST模型 8450 −32.38 −7.88 −9.38 11299 −22.90 −4.92 −1.43 12653 −22.11 6.64 0.48 方均根 22.70 5.71 4.75 表 4 边界条件及工质物性
Table 4. Boundary conditions and coolant physical properties
项目 参数 数值 典型工况 实验工况范围 进口 $ \dot m $/(kg/(s·m2)) 1.77 0.47~2.13 T0/K 302.92 296.12~306.25 出口 p4/kPa 102.89 102.81~103.01 T4/K 297.15 297.15 工质
物性μ/10−6 (kg/(m·s)) 1.88 1.84~1.89 ρspec/(kg/m3) 1.26 1.20~1.28 λ/(W/(m·K)) 0.026 0.026~0.027 cp/(kJ/(kg·K)) 1.005 1.005 表 5 典型位置中截面$ \overline {{\boldsymbol{p}}_{{\bf{s}}}^{\boldsymbol{*}}/{\boldsymbol{p}}_{{{\boldsymbol{0}} {\bf{s}}}}^{\boldsymbol{*}}} $
Table 5. $ \overline {{\boldsymbol{p}}_{{\bf{s}}}^{\boldsymbol{*}}/{\boldsymbol{p}}_{{{\boldsymbol{0}} {\bf{s}}}}^{\boldsymbol{*}}} $ on middle section of typical locations
结构类型 进气孔 夹层 气膜孔 典型层板结构 0.9986 0.9696 0.9595 蜂巢式结构 0.9979 0.9808 0.9700 表 6 实验件结构参数
Table 6. Structure parameters of 2 test parts
结构类型 参数 数值 典型层板结构 蜂巢式结构 实验件
整体H1/mm 1.26 H2/mm 1.31 H3/mm 1.90 A0/mm2 2128.34 2021.93 A3/mm2 41.43 39.41 n/个 20 19 单元体 b/mm 0.93 e/mm 2.53 c/mm 0.83 $ \delta $/mm 0.93 L/mm 10.32 6.40 ϕd1/mm 1.62 ϕd2/mm 3.60 5.09 ϕd3/mm 1.62 α/(°) 90 35 β/(°) 35 -
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