摘要
对降液管结构进行了优化设计 ,并在此基础上提出了一种新型塔板 ,即DOS塔板。试验研究结果表明 。
Based on the actual need of distillation process,a optimized structure of downcomer and a new type of tray——DOS tray is carried out in order to use free area more efficiently on column tray.On a semi cylindrical tray simulator(1.6?m diameter),the hydraulic performance of DOS tray is studied.The results indicate that the pressure drop per tray,the height of clear liquid on tray,weeping and entrainment rate are lower than those of the normal tray.
出处
《石油化工设备》
CAS
2001年第B05期24-26,共3页
Petro-Chemical Equipment