Cooling characteristics of liquid ammonia for hypersonic solid-fueled scramjet
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摘要:
拟使用液氨作为新型氮基燃料再生冷却剂,考虑超燃冲压发动机真实工作温度和压力参数,建立三维流动传热裂解模型,分析液氨流动传热特性,并与传统碳氢燃料进行对比。利用PR状态方程和Chung方法,描述液氨和正癸烷的物性参数;基于Lee蒸发模型,计算冷却剂的相变;基于液氨与正癸烷的简化裂解机理,建立再生冷却通道中流体的流动传热裂解模型。数值研究了不同温度、压力下液氨的流动传热特性;对比分析相同条件下,液氨与碳氢燃料的热沉规律。结果表明液氨传热能力随压力上升而提升,压力由3 MPa提升至17 MPa时,平均表面传热系数增幅8.02%;相同质量流量下,以液氨作为冷却剂将大幅提升冷却能力,非裂解区最高壁温降幅度36.3%,裂解区为9.1%。
Abstract:Liquid ammonia is used as a new nitrogen-based coolant. Considering the real operating temperature and pressure of the scramjet engine, a three-dimensional numerical model was established to analyze the flow and heat transfer characteristics of liquid ammonia. The thermal properties were calculated by PR equation and Chung method. The phase change of ammonia was calculated by Lee evaporation model. Pyrolysis of ammonia was also considered. The flow heat transfer characteristics of liquid ammonia under different temperatures and pressures were studied by taking into account the process of phase change and pyrolysis. The cooling feature of ammonia was compared with traditional hydrocarbon fuel. The heat sink of liquid ammonia and hydrocarbon fuel was compared and analyzed under the same condition. The results showed that the heat transfer capacity of liquid ammonia increased with the rise of pressure. When pressure increased from 3 MPa to 17 MPa, heat transfer coefficient increased by 8.02%. Under the same mass flow rate, heat transfer coefficient of ammonia was higher and the wall temperature decreased by 36.3% in non-pyrolysis zone and 9.1% in pyrolysis zone.
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Key words:
- ammonia /
- hydrocarbon fuel /
- cooling feature /
- flow and heat transfer /
- pyrolysis /
- high Mach number /
- solid-fueled scramjet
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表 1 单矩形通道网格无关性验证相关信息
Table 1. Single rectangular channel mesh independence verification related information
网格
编号首层网格
厚度/m比例
因子y+ 网格数/106 Tout,av/K Mesh A 10−5 1.15 < 1 1.994 480.2 Mesh B 2.961 475.8 Mesh C 4.516 473.4 Mesh D 6.715 473.2 表 2 不同压力下的边界条件参数
Table 2. Boundary conditions under different pressures
qf/(MW/m2) mf/(g/s) pout/MPa 2 2.75 3 2 2.75 6 2 2.75 9 2 2.75 13 2 2.75 15 2 2.75 17 表 3 不同工况下的边界条件参数
Table 3. Boundary condition parameters under different working conditions
工况 qf/
(MW/m2)mf/
(g/s)(qf/mf)/
(W·s/(kg·m2))pout/
MPaCase a 2.0 3.00 0.667 3 Case b 2.0 2.75 0.727 3 Case c 2.5 2.75 0.909 3 Case d 3.0 2.75 1.091 3 表 4 氨和碳氢燃料冷却能力对比分析计算工况
Table 4. Calculation conditions in the comparison of cooling capacities between ammonia and hydrocarbon fuel
Case 流体种类 Tin/
Kmf/
(g/s)pout/
MPaqf/
(MW/m2)1 NH3 300 2.75 3 2 2 C10H22 300 2.75 3 2 3 NH3 680 2.75 3 2 4 C10H22 680 2.75 3 2 -
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