摘要
在塔径０１１２ｍ的三组不同直径导流管装置中。
Gas hold-up was measured for foaming and non-Newtonian solutions in a 0 112 m diameter bubble column with a draft-tube of different size The gas hold-up was determined using the liquid overflow method The influence of superficial gas velocity and the ratio of the draft-tube diameter to column diameter on gas hold-up was analyzed
出处
《化工冶金》
CSCD
北大核心
1997年第4期354-357,共4页
