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系统输送压力对于He Ⅱ强制流动输送系统而言至关重要,因此在系统运行之前,实现对其数值的有效预测是一项十分必要而有意义的工作.根据特定管路结构所能允许的均匀极限漏热量,借助于具有一定实验基础的经典流体紊流流动关系式,可以预测能够成功实现He Ⅱ传输的系统压力差.

参考文献

[1] Dresner L;Kashani A;Sciver S W Van .Studies of Heat Transport to Forced Flow He Ⅱ[J].Cryogenics,1986,26(02):111-113.
[2] Li Yanzhong;Wu Yuyuan;Wu Yezheng .Correlations for Calculating Thermal Properties of Superfluid Helium[J].Cryogenics and superconductivity,1996,24(01):34-39.
[3] Thermodynamic;Transport.Superfluid,Lamda Line Properties of Helium for Temperature from 0.8 K to 1500 K with Pressure to 20000 Bars Including Liquid-VaporMixture[M].Cryodata,HEPAK
[4] Sciver S W Van.Heat Transfer in Superfluid Helium Ⅱ[A].Westbury:IPC Science and Technology,1980:228-237.
[5] Sciver S W Van .Heat Transport in Forced Flow He Ⅱ:Analytic Solution[J].Advances in Cryogenic Engineering,1984,29:315-322.
[6] Sciver S W Van .Transient Heat Transport in He Ⅱ[J].Cryogenics,1979,19(07):385-392.
[7] Kashani A;Sciver S W Van .Steady State Forced Convection Heat Transfer in He Ⅱ[J].Advances in Cryogenic Engineering,1986,31:489-498.
[8] Kashani A;Sciver S W Van .Numerical Solution of Forced Convection Heat Transfer in He Ⅱ[J].Numerical Heat Transfer Part A-Applications,1989,16(02):213-228.
[9] Rousset B;Claudet G;Gauthier A et al.Pressure Drop and Transient Heat Transport in Forced Flow Single Phase Helium Ⅱ at High Reynolds Number[J].Cryogenics,1994,34(zk):317-320.
[10] Walstrom P L;Weisend Ⅱ J G;Maddocks J R et al.Turbulent Flow Pressure Drop in Various He Ⅱ Transfer System Components[J].Cryogenics,1988,28(02):101-109.
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