Morphodynamics of flow-sediment-structure interaction and flow pattern visualization

2020 ◽  
Vol 1504 ◽  
pp. 012006
Author(s):  
Rakesh Kumar ◽  
Salil Khana ◽  
Abhishek Kumar Tiwari ◽  
Dharmendra Tripathi ◽  
Niti Nipun Sharma

2012 ◽  
Vol 11 (2) ◽  
pp. 117
Author(s):  
PRIYO HERU ADIWIBOWO

Multi-phase flows are widely encountered in several engineering and industrial facilities, such as conventional steam power  plants, evaporators and condensers, pressurized-water nuclear reactors, a wide variety of petroleum industries, chemicals and  food processing industries. Surely, in the complex pipeline  installation of these systems, vertical pipe will be commonly  used for pipe connection. The purpose of this work is to investigate the flow pattern of gas-liquid two phase in the vertical pipe. Experiments will be performed in a 36 mm ID  acrylic pipe vertical. Superifical liquid velocities and volumetric gas quality will be varied 0.3~1,1 m/s and 0.05~0.2 respectively. Digital camera will be used for flow pattern  visualization in the vertical pipe. It was observed that effect of vertical pipe on flow pattern formed cluster bubbly flow for low volumetric gas quality with high superifical liquid velocities. For  superifical liquid velocities with medium volumetric gas quality formed homogeneous bubbly flow and high volumetric gas quality is dense bubbly flow.


2015 ◽  
Vol 2015.21 (0) ◽  
pp. _10112-1_-_10112-2_ ◽  
Author(s):  
Kenji AMAGAI ◽  
Yoshihiro KIYAMA ◽  
Akira FUKUNAGA ◽  
Hirokuni HIYAMA ◽  
Satomi HAMADA

2005 ◽  
Vol 89 (6) ◽  
pp. 719-732 ◽  
Author(s):  
Mehul S. Vesvikar ◽  
Muthanna Al-Dahhan

2018 ◽  
Vol 58 (2) ◽  
pp. 1075-1086 ◽  
Author(s):  
Enrique A. López-Guajardo ◽  
Gabriela M. Garza-Cantú ◽  
André Marques-Camarena ◽  
Enrique Ortiz-Nadal ◽  
Krishna D.P. Nigam ◽  
...  

2005 ◽  
Vol 52 (1-2) ◽  
pp. 537-543 ◽  
Author(s):  
M.S. Vesvikar ◽  
R. Varma ◽  
K. Karim ◽  
M. Al-Dahhan

Advanced non-invasive experiments like computer automated radioactive particle tracking and computed tomography along with computational fluid dynamics (CFD) simulations were performed in mimic anaerobic digesters to visualize their flow pattern and obtain hydrodynamic parameters. The mixing in the digester was provided by sparging gas at three different flow rates. The simulation results in terms of overall flow pattern, location of circulation cells and stagnant regions, trends of liquid velocity profiles, and volume of dead zones agree reasonably well with the experimental data. CFD simulations were also performed on different digester configurations. The effects of changing draft tube size, clearance, and shape of the tank bottoms were calculated to evaluate the effect of digester design on its flow pattern. Changing the draft tube clearance and height had no influence on the flow pattern or dead regions volume. However increasing the draft tube diameter or incorporating a conical bottom design helped in reducing the volume of the dead zones as compared to a flat bottom digester. The simulations showed that the gas flow rate sparged by a single point (0.5 cm diameter) sparger does not have appreciable effect on the flow pattern of the digesters.


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