火箭推进

板式表面张力贮箱导流板的理论计算与试验验证

邱中华^1,2,刘志杰^1,2,朱文杰^1,2,黄立钠^1,2,陈志坚^1,2

(1.上海空间推进研究所,上海 201112; 2.上海空间发动机工程技术研究中心,上海 201112)

Theoretical calculation and experimental verification of vanes using in vane type surface tension tank

QIU Zhonghua^1,2, LIU Zhijie^1,2, ZHU Wenjie^1,2, HUANG Lina^1,2, CHEN Zhijian^1,2

(1.Shanghai Institute of Space Propulsion, Shanghai 201112, China; 2.Shanghai Engineering Research Center of Space Engine, Shanghai 201112, China)

Keywords：surface tension tank; vane; theoretical calculation; neutral buoyancy test; experimental verification

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参考文献

板式表面张力贮箱的PMD通常包括导流板与出口附近的蓄液器,导流板是影响板式贮箱性能的关键因素之一,由于地面没有失重环境无法直接进行导流板的工作原理地面验证。为了确认导流板的可用性,通过理论分析建立了导流板液体传输能力的计算方法,通过中性浮力试验对导流板的液体收集能力进行了试验验证。经过多次试验的试验结果与理论计算结果的对比分析,得到了一种可应用于工程设计的计算方法,利用该方法编程形成了一套计算软件,可指导板式表面张力贮箱内导流板的设计。

Vane type surface tension tank's PMD usually include vanes at wall and liquid reservoir at outlet.Vane is a critical component on liquid collecting capacity, but this cannot be verificated at the ground condition because without microgravity condition.In order to verify the usability of vans, theoretical calculation method for liquid transportation ability of vane was built.Then neutral buoyancy test was conducted to validate liquid collection capacity of vane.The experimental verification result was contrasted with theoretical calculation result, and a calculation method sutiable for engineering design was obtained.Finally a vane computing software was formed to direct the vanes design in vane type surface tension tank.

引言
1 导流板液体传输原理
2 导流板液体传输能力理论计算
3 针对导流板的中性浮力试验
4 工程可用的导流板计算方法
5 结语

图1 位于斜面上的导流板的液带分布<br/>Fig.1 Fillet on the vane at the incline

图1 位于斜面上的导流板的液带分布
Fig.1 Fillet on the vane at the incline

图2 单竖片式导流板截面形状<br/>Fig.2 Simple vane cross section

图2 单竖片式导流板截面形状
Fig.2 Simple vane cross section

图3 原理型板式贮箱示意图<br/>Fig.3 A schematic diagram of vane type tank

图3 原理型板式贮箱示意图
Fig.3 A schematic diagram of vane type tank

图4 原理型贮箱导流板理论计算结果<br/>Fig.4 Theoretical calculation result of a vane in a principle vane type tank

图4 原理型贮箱导流板理论计算结果
Fig.4 Theoretical calculation result of a vane in a principle vane type tank

图5 两种介质的密度关系<br/>Fig.5 Density relationship of two medium

图5 两种介质的密度关系
Fig.5 Density relationship of two medium

表1 模拟的加速度值与温度的关系<br/>Tab.1 Acceleration simulated by temperature

表1 模拟的加速度值与温度的关系
Tab.1 Acceleration simulated by temperature

图6 试验用导流板结构形式<br/>Fig.6 Vane structure for the experiment

图6 试验用导流板结构形式
Fig.6 Vane structure for the experiment

图7 中性浮力试验贮箱实物图(0.027 5 m/s2)<br/>Fig.7 The tank used in buoyancy experiment(0.027 5 m/s2)

图7 中性浮力试验贮箱实物图(0.027 5 m/s2)
Fig.7 The tank used in buoyancy experiment(0.027 5 m/s2)

表2 试验数据表<br/>Tab.2 Experiment data 单位:mm

表2 试验数据表
Tab.2 Experiment data 单位:mm

图8 理论计算各物理量关系示意图<br/>Fig.8 The relationship of parameters for the calculation

图8 理论计算各物理量关系示意图
Fig.8 The relationship of parameters for the calculation

图9 试验结果与计算结果对比(0.027 5 m/s2)<br/>Fig.9 Contrast of experiment and calculation results(0.027 5 m/s2)

图9 试验结果与计算结果对比(0.027 5 m/s2)
Fig.9 Contrast of experiment and calculation results(0.027 5 m/s2)

图10 中性浮力试验贮箱实物图(0.007 m/s2)<br/>Fig.10 The tank used in buoyancy experiment(0.007 m/s2)

图10 中性浮力试验贮箱实物图(0.007 m/s2)
Fig.10 The tank used in buoyancy experiment(0.007 m/s2)

图11 试验结果与计算结果对比(0.007 m/s2)<br/>Fig.11 Contrast of experiment and calculation results(0.007 m/s2)

图11 试验结果与计算结果对比(0.007 m/s2)
Fig.11 Contrast of experiment and calculation results(0.007 m/s2)

图12 中性浮力试验贮箱实物图(0.036 7 m/s2)<br/>Fig.12 The tank used in buoyancy experiment(0.036 7 m/s2)

图12 中性浮力试验贮箱实物图(0.036 7 m/s2)
Fig.12 The tank used in buoyancy experiment(0.036 7 m/s2)

图13 试验结果与计算结果对比(0.036 7 m/s2)<br/>Fig.13 Contrast of experiment and calculation results(0.036 7 m/s2)

图13 试验结果与计算结果对比(0.036 7 m/s2)
Fig.13 Contrast of experiment and calculation results(0.036 7 m/s2)

图14 中性浮力试验贮箱实物图(0.039 4 m/s2)<br/>Fig.14 The tank used in buoyancy experiment(0.039 4 m/s2)

图14 中性浮力试验贮箱实物图(0.039 4 m/s2)
Fig.14 The tank used in buoyancy experiment(0.039 4 m/s2)

图15 试验结果与计算结果对比(0.039 4 m/s2)<br/>Fig.15 Contrast of experiment and calculation results(0.039 4 m/s2)

图15 试验结果与计算结果对比(0.039 4 m/s2)
Fig.15 Contrast of experiment and calculation results(0.039 4 m/s2)

图16 中性浮力试验贮箱实物图(0.040 4 m/s2侧向)<br/>Fig.16 The tank used in buoyancy experiment(0.040 4 m/s2 lateral)

图16 中性浮力试验贮箱实物图(0.040 4 m/s2侧向)
Fig.16 The tank used in buoyancy experiment(0.040 4 m/s2 lateral)

图17 试验结果与计算结果对比(0.040 4 m/s2侧向)<br/>Fig.17 Contrast of experiment and calculation results(0.040 4 m/s2 lateral)

图17 试验结果与计算结果对比(0.040 4 m/s2侧向)
Fig.17 Contrast of experiment and calculation results(0.040 4 m/s2 lateral)

表3 试验结果统计表
Tab.3 Experiment results

图18 软件界面<br/>Fig.18 The software interface

图18 软件界面
Fig.18 The software interface

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期刊信息

火箭推进
JOURNAL OF ROCKET PROPULSION

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标准刊号 ISSN 1672-9374
CN 61-1436/V

备注

引言

1 导流板液体传输原理

2 导流板液体传输能力理论计算

3 针对导流板的中性浮力试验

4 工程可用的导流板计算方法

5 结语

期刊信息