Power Consumption and Mass Transfer of High Viscosity Liquid in Gas–Liquid Mixing Vessel with Large Paddle Impeller

2016 ◽  
Vol 42 (5) ◽  
pp. 174-178
Author(s):  
Masahiro Haitsuka ◽  
Noboru Kamei ◽  
Yoshihito Kato ◽  
Masataka Kamiya ◽  
Haruki Furukawa ◽  
...  
2014 ◽  
Vol 40 (5) ◽  
pp. 372-375
Author(s):  
Noboru Kamei ◽  
Yoshihito Kato ◽  
Ryo Nagumo ◽  
Haruki Furukawa ◽  
Tomoya Suzuki ◽  
...  

2012 ◽  
Vol 38 (4) ◽  
pp. 209-211 ◽  
Author(s):  
Haruki Furukawa ◽  
Eiki Oda ◽  
Chengli He ◽  
Noboru Kamei ◽  
Yoshihito Kato ◽  
...  

Author(s):  
Dr. Mazhar Hussain

The hydrodynamic characteristics of mixing fluids are always the points to consider in improvement of their mixing quality especially using motionless mixers normally stated as “Static Mixers”. Motionless mixing technique was adopted for Air-Water system with the advantage of negligible power consumption over dynamic mixers. Different hydrodynamic characteristics were experimented using “Baffle Type” static element and were compared to those of already used in recent studies. Dissolved oxygen content, Static mixer geometry (i.e. Baffle, Blade, Wheel, Plate and Needle), mixing fluids flow rates were chosen as variables and selected in this content as rate of mass transfer study which founds out to be significant using “Baffle Type” static element. Volumetric mass transfer was also achieved at higher scale which gives a clear indication of increase the mass transfer coefficient in between the comparison of “Baffle type” element and other mentioned elements. Pressure droplet and depletion in Air bubble size across static elements were visually perceived using Hg-Manometer and still photography respectively. A mathematical model was also developed portraying the Air bubble diameter at different flow rates for this system. Other hydrodynamics like higher Dissolved Oxygen (DO) Content, Less Power consumption were also found to be more advantageous for “Baffle Type” static element.


Fuel ◽  
2019 ◽  
Vol 235 ◽  
pp. 1327-1336 ◽  
Author(s):  
Kiarash Keshmiri ◽  
Mohammad Pourmohammadbagher ◽  
Haibo Huang ◽  
Neda Nazemifard

Author(s):  
Deyin Gu ◽  
Fenghui Zhao ◽  
Xingmin Wang ◽  
Zuohua Liu

Abstract The solid-liquid mixing characteristics in a stirred tank with pitched blade impellers, dislocated impellers, and dislocated guide impellers were investigated through using CFD simulation. The effects of impeller speed, impeller type, aperture ratio, aperture length, solid particle diameter and initial solid holdup on the homogeneity degree in the solid-liquid mixing process were investigated. As expected, the solid particle suspension quality was increased with an increase in impeller speed. The dislocated impeller could reduce the accumulation of solid particles and improve the cloud height compared with pitched blade impeller under the same power consumption. The dislocated guide impeller could enhance the solid particles suspension quality on the basis of dislocated impeller, and the optimum aperture ratio and aperture length of dislocated guide impeller were 12.25% and 7 mm, respectively, in the solid-liquid mixing process. Smaller solid particle diameter and lower initial solid holdup led to higher homogeneity degree of solid-liquid mixing system. The dislocated guide impeller could increase solid particle integrated velocity and enhance turbulent intensity of solid-liquid two-phase compared with pitched blade impeller and dislocated impeller under the same power consumption.


Author(s):  
Le Xie ◽  
Qi-An Wang ◽  
Xian-Jin Luo ◽  
Zheng-Hong Luo

Abstract Solid particle dispersion and chemical reactions in high-viscosity non-Newtonian fluid are commonly encountered in polymerization systems. In this study, an interphase mass transfer model and a finite-rate/eddy-dissipation formulation were integrated into a computational fluid dynamics model to simulate the dispersion behavior of particles and the mass transfer–reaction kinetics in a condensation polymerization-stirred tank reactor. Turbulence fields were obtained using the standard k–ε model and employed to calculate the mixing rate. Cross model was used to characterize the rheological property of the non-Newton fluid. The proposed model was first validated by experimental data in terms of input power. Then, several key operating variables (i.e. agitation speed, viscosity, and particle size) were investigated to evaluate the dispersive mixing performance of the stirred vessel. Simulation showed that a high agitation speed and a low fluid viscosity favored particle dispersions. This study provided useful guidelines for industrial-scale high-viscosity polymerization reactors.


2020 ◽  
Vol 10 (2) ◽  
pp. 449-459 ◽  
Author(s):  
Alireza Bordbar ◽  
Sasan Kheirandish ◽  
Arsalan Taassob ◽  
Reza Kamali ◽  
Amin Ebrahimi

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