文献类型：期刊文献

英文题名：Hydrodynamics of an Airlift Column for Aeration in Molten Sulfur

作者：Wang, Junjie[1];Xu, Xiao[1];Wang, Wei[1];Li, Yudong[1];Wu, Shihan[1];Yang, Haiqiang[1];Yang, Qiang[1,2]

机构：[1]East China Univ Sci & Technol, Sch Mech & Power Engn, Shanghai 200237, Peoples R China;[2]East China Univ Sci & Technol, Natl Engn Lab Ind Wastewater Treatment, Shanghai 200237, Peoples R China

年份：2022

卷号：12

期号：1

外文期刊名：APPLIED SCIENCES-BASEL

收录：;WOS:【SCI-EXPANDED(收录号:WOS:000741852600001)】；

基金：FundingThis research was funded by the National Natural Science Foundation of China (51678238, 51722806, 51608325, 21908057); the National Key R&D Program of China (2018YFC1802704, 2018YFC1801904); and the Shanghai Sailing Program (19YF1411800).

语种：英文

外文关键词：internal loop airlift column; molten sulfur; CFD simulation; gas holdup; bubble diameter; liquid circulation velocity

摘要：The airlift column is a promising technology for the removal of volatile gas from high-viscosity molten sulfur. However, a detailed analysis is lacking on the hydrodynamic properties inside the column, due to the difficulty in flow behavior detection in the opaque molten sulfur. In this work, we adopted the computational fluid dynamics simulation to understand the hydrodynamic behaviors in an airlift column for molten sulfur aeration. In addition, we analyzed the impacts of the superficial gas velocity (U-Gr) and column height on the hydrodynamic characteristics, such as gas holdup, average bubble diameter, and liquid circulation velocity (U-Lr) in the column. The simulation shows that at a constant column height of 15 m, an increase on gas holdup can be obtained with the increase of the superficial gas velocity, while the bubble diameter remains almost constant. Once the superficial gas velocity exceeded 0.333 m/s, the liquid circulation velocity increased slowly. With a variation on the column height from 5 to 25 m, a negligible change on gas holdup, but an obvious increase on liquid circulation velocity and bubble diameter is observed at the given superficial gas velocity of 0.0389 m/s. Furthermore, the simulation shows a similar trend, but with considerably more detailed information, on the relationship between the gas holdup and liquid circulation velocity when compared to the predictions from the Chisti correlation (1988) and an optimized correlation proposed in this work.