摘要
建立了湿蒸汽凝结流动的理论模型,并利用经典实验结果对该模型进行了校验,验证了模型的准确性。在此基础上,对不同结构参数下环型引射流场内的水蒸气凝结流动过程进行了数值仿真。结果表明:适当地减小收敛比、面积比α和增大二次喉道的长径比l/d,可以提高总压恢复系数,改善引射器性能。
The theoretical model for wet steam condensation flow was established. Furthermore, numerical simulation results with wet steam condensation flow model were coincident to the experimental data of C. A. Moses, which validated the credibility and accuracy of the model. Then, numerical simulation on condensation flow process was carried out under different configuration parameters. The results show that appropriately reducing the convergence ratio ~, area ratio and increasing the l/d of secondary throat can increase the total pressure recovery coefficient, which improves the ejector performance.
出处
《国防科技大学学报》
EI
CAS
CSCD
北大核心
2011年第3期10-13,32,共5页
Journal of National University of Defense Technology
基金
国家安全重大基础研究项目(613102)
关键词
环型蒸汽引射器
湿蒸汽
凝结
数值模拟
annular vapour ejector
wet steam
condensation
numerical simulation