Abstract

The hydrodynamics parameters of microbubbles in a bubble column were studied in an air–water system with a range of superficial gas velocity from 0.013 to 0.100 m/s using a differential pressure transmitter, double probe optical fiber probe, and electrical resistance tomography (ERT) technique. Two kinds of microbubble generators (foam gun, sintered plate) were used to generate microbubbles in the bubble column with a diameter of 90 mm, and to compare the effects of different foaming methods on the hydrodynamics parameters in the bubble column. The hydrodynamic behavior of the homogeneous regime and the transition regime was also studied. The results show that, by changing the microbubble-generating device, the hydrodynamic parameters in the column are changed, and both microbubble-generating devices can obtain a higher gas holdup and a narrower chord length distribution. When the foam gun is used as the gas distributor, a higher gas holdup and a narrower average bubble chord length can be obtained than when the sintered plate is used as the gas distributor. In addition, under different operating conditions, the relative frequency distribution of the chord length at different radial positions is mainly concentrated in the interval of 0–5 mm, and it is the highest in the center of the column.

Highlights

  • The bubble column reactor is widely used in gas–liquid reaction systems such as chemical, petrochemical, sewage treatment, mineral processing, and biochemical industries [1,2,3,4,5], due to its simple internal structure, easy operation, and maintenance

  • The superficial gas velocity ranged from 0.013 to 0.100 m/s, and when using a foam gun and a sintered plate as the gas distributors, microbubbles will be generated in the bubble column, and the change trend of gas holdup is similar to the literature [21,22]

  • By comparing the two gas distributors, it can be found that when the sintered plate is used as the gas distributor, the gas holdup is higher before 0.04 m/s and the gas holdup of plane 2 is higher than plane 1, mainly due to plane 2 being closer to the distributor

Read more

Summary

Introduction

The bubble column reactor is widely used in gas–liquid reaction systems such as chemical, petrochemical, sewage treatment, mineral processing, and biochemical industries [1,2,3,4,5], due to its simple internal structure, easy operation, and maintenance. The correct design and operation of these devices depend on the convection type and understanding of global and local properties (gas holdup, bubble chord length distribution). The flow regime is closely related to the superficial gas velocity, bubble column diameter, and initial liquid level height, etc. The bubble rising velocity and the choice of gas distributor have a great influence on the flow regime. At a low superficial gas velocity, coalescence and breakup of bubbles rarely occurs; the design of the gas Processes 2020, 8, 663; doi:10.3390/pr8060663 www.mdpi.com/journal/processes

Objectives
Results
Conclusion
Full Text
Published version (Free)

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call