Simulation and Experiment of Residence Time Distribution in Short-Contact Cyclone Reactors

2014 ◽  
Vol 672-674 ◽  
pp. 1622-1625
Author(s):  
Yu Chun Zhang ◽  
Wei Zou

The Eulerian-Eulerian model and species transport method were used for the residence time distribution (RTD) predictions of the short-contact cyclone reactor. A video camera and colored particle tracer were employed in the experiment. The component concentration distribution and RTD characteristics were analyzed. The results indicate that the vacuum gas oil (VGO) and catalysts flow down spirally along the wall and the gasoline and dry gas are mostly in the central part, so the VGO has more contact time with catalysts than other gas components. The RTDs indicate that there exists vortex, backflow and other secondary flow in the reactor. The simulated results show a good agreement with the experimental data.

2015 ◽  
Vol 26 (4) ◽  
pp. 1134-1142 ◽  
Author(s):  
Yuchun Zhang ◽  
Zhenbo Wang ◽  
Youhai Jin ◽  
Zhihe Li ◽  
Weiming Yi

2021 ◽  
Vol 32 (2) ◽  
pp. 611-618
Author(s):  
Atena Dehghani Kiadehi ◽  
Mikel Leturia ◽  
Franco Otaola ◽  
Aissa Ould-Dris ◽  
Khashayar Saleh

Metals ◽  
2021 ◽  
Vol 11 (3) ◽  
pp. 430
Author(s):  
Changyou Ding ◽  
Hong Lei ◽  
Hong Niu ◽  
Han Zhang ◽  
Bin Yang ◽  
...  

The residence time distribution (RTD) curve is widely applied to describe the fluid flow in a tundish, different tracer mass concentrations and different tracer volumes give different residence time distribution curves for the same flow field. Thus, it is necessary to have a deep insight into the effects of the mass concentration and the volume of tracer solution on the residence time distribution curve. In order to describe the interaction between the tracer and the fluid, solute buoyancy is considered in the Navier–Stokes equation. Numerical results show that, with the increase of the mass concentration and the volume of the tracer, the shape of the residence time distribution curve changes from single flat peak to single sharp peak and then to double peaks. This change comes from the stratified flow of the tracer. Furthermore, the velocity difference number is introduced to demonstrate the importance of the density difference between the tracer and the fluid.


Sign in / Sign up

Export Citation Format

Share Document