液氢贮箱加注-保持-排气式预冷特性及影响因素研究

Research on the Chilldown Characteristics and Influencing Factors of the Charge-Hold-Vent Method for Liquid Hydrogen Tank

  • 摘要: 为研究微重力条件下低温推进剂贮箱的加注-保持-排气式(CHV)预冷特性,选择液氢贮箱作为对象,建立CHV预冷全过程热平衡数值模型,计算并分析预冷过程温度、压力及沸腾传热特性,研究加注质量流速、排气目标压力及气壁温差最小限值对预冷性能的影响规律。结果表明:CHV预冷前期对低温流体冷却能力利用不足,更易引发超压风险;CHV预冷周期内加注、保持和排气阶段壁面降温速率逐渐减小;液壁间沸腾传热集中发生于加注阶段,该阶段预冷全程以膜沸腾传热为主,平均时间占比达91%;适当增加加注质量流速和气壁温差限值可有效改善CHV预冷性能,其中质量流速从0.01 kg/s提高至0.05 kg/s时,壁面降温速率提升4.9倍,预冷消耗时长降低6.9%,气壁温差限值从5 K增加至20 K时,预冷消耗时长降低38%,消耗质量仅增加10%。

     

    Abstract: In order to study the chilldown characteristics of the Charge-Hold-Vent (CHV) process for cryogenic propellant tanks under microgravity conditions, a liquid hydrogen (LH2) tank was selected as the research object. A thermal balance numerical model covering the entire CHV chilldown process was established to calculate and analyze the temperature, pressure, and boiling heat transfer characteristics during chilldown. The effects of the filling mass flow rate, initial tank pressure and the minimum limit value of gas-wall temperature difference on the chilldown process and performance were investigated. The results show that: the prediction results of the present model for the tank pressure and wall temperature throughout the entire chilldown process show good agreement with the simulation data from the Honkonen model, demonstrating its capability to achieve accurate predictions of the CHV chilldown characteristics of the LH2 tank; In the early stage of CHV chilldown, the chilldown capacity of cryogenic fluid is insufficiently utilized, and there is a greater risk of overpressure. The wall chilldown rate gradually decreases in the charge, hold and vent stages of the CHV cycle. During the initial phase of CHV tank chilldown, film boiling dominates the boiling heat transfer between the liquid and the wall, which later gradually transitions to being primarily characterized by transition boiling. Furthermore, the boiling heat transfer at the liquid-wall interface is concentrated in the charge stage of each CHV cycle. Throughout this stage, film boiling remains the predominant mode of heat transfer, accounting for an average time proportion of 91% over the entire chilldown process. Appropriately increasing the mass flow rate and the allowable gas-wall temperature difference can effectively improve the chilldown performance of CHV. When the mass flow rate is increased from 0.01 kg/s to 0.05 kg/s, the wall chilldown rate increases by 4.9 times, and the total chilldown consumption time is reduced by 6.9%. When the allowable gas-wall temperature difference is increased from 5 K to 20 K, the total chilldown consumption time is reduced by 38%, while the propellant consumption increases by only 10%.

     

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