Hydrodynamic analysis of a banbury mixer 2-D flow simulations for the entire mixing chamber

1989 ◽  
Vol 29 (15) ◽  
pp. 1059-1065 ◽  
Author(s):  
Jing-Jy Cheng ◽  
Ica Manas-Zloczower
Author(s):  
Ilyoup Sohn ◽  
Hae Yoon Jeong

A microorganism incubator has been developed by a prototype performance tests and computational fluid dynamics (CFD) simulations. The microorganism incubator is useful to supply the high quality of fertilizer to agricultural industries. Particularly, a small-sized, movable incubator is desired to be produced for personal agriculturalists. Since the incubator is basically designed as a type of mixing tank for mixing water and powder of microorganism, the decision of an impeller type and size, positions, size of internal parts such as baffles for an efficient mixing process should be considered. To produce the effect of turbulence on the efficient mixing, the location and size of baffles on the chamber wall is particularly significant to the mixing chamber design process. Multiphase CFD simulations are performed to describe the mixing flows inside the tank and the flow physics and patterns are studied in order to find out the optimal conditions for the microorganism incubating. Since water with powder of microorganism is partially filled with the chamber, air-water two phase flows should be considered in the CFD simulation. To simulate such flows, the volume of fluid (VOF) scheme is used. Both steady-state and time-transient simulations are performed and their results between two different time derivative considerations are compared, which enables us to clearly understand the effects of unsteady flow characteristics on the whole flow phenomena in the chamber. Additionally, comparisons of the turbulence modeling for the rotating flows in the chamber will be performed to describe the complex flow phenomena around the rotating impeller and the stationary baffles on the chamber wall. Prior to performing CFD study for the real type of the chamber, the flow simulations for the mixing chamber whose flow characteristics were already studied by experiments are performed with respect to the change of the turbulence modeling and numerical methods. Thus, the proper numerical methods and turbulent modeling are then determined. After validations of the turbulent modeling and numerical schemes, the flow phenomena occurred at the real prototype of the microorganism chamber corresponding to the change of design parameter of the chamber such as the change of the chamber bottom shape, an impeller blade length and the number of baffles will be analyzed.


Author(s):  
S. P. Eron’ko ◽  
M. Yu. Tkachev ◽  
E. V. Oshovskaya ◽  
B. I. Starodubtsev ◽  
S. V. Mechik

Effective application of slag-forming mixtures (SFM), being fed into continuous castingg machine (CCM) moulds, depends on their even distribution on the melt surface. Manual feeding of the SFM which is widely usedd does not provide this condition, resulting in the necessity to actualize the work to elaborate systems of SFM mechanized feedingg into moulds of various types CCM. A concept of the designing of a system of SFM feeding into CCM moulds presented with the ratte strictly correspondent to the casting speed and providing formation of an even layer of fine material of given thickness on the whoole surface of liquid steel. The proposed methods of designing of the SFM mechanized feeding systems based on three-dimensional computer simulation with the subsequent verification of the correctness of the adopted technical solutions on field samples. Informattion is presented on the design features of the adjusted facilities intended for continuous supply of finely granulated and powder mixtuures on metal mirror in moulds at the production of high-quality billets, blooms and slabs. Variants of mechanical and pneumo-mechaanical SFM supply elaborated. At the mechanical supply the fine material from the feeding hopper is moved at a adjusted distance bby a rigid horizontally located screw. At the pneumo-mechanical supply the metered doze of the granular mixture is delivered by a sshort vertical screw, the lower part of which is located in the mixing chamber attached from below to the hopper and equipped with ann ejector serving for pneumatic supply of the SFM in a stream of transporting gas. It was proposed to use flexible spiral screws in the ffuture facilities of mechanical SFM feeding. It will enable to eliminate the restrictions stipulated by the lack of free surface for locatiion of the facility in the working zone of the tundish, as well as to decrease significantly the mass of its movable part and to decreaase the necessary power of the carriage moving mechanism driver. The novelty of the proposed technical solutions is protected by thhree patents. The reduction of 10–15% in the consumption of slag-forming mixtures during the transition from manual to mechanizeed feeding confirmed. The resulting economic effect from the implementation of technical development enables to recoup the costs inncurred within 8–10 months.


1987 ◽  
Author(s):  
N. YU ◽  
K. KUSUNOSE ◽  
H. CHEN ◽  
D. SOMMERFIELD

2001 ◽  
Author(s):  
Edward Luke ◽  
Xiao-Ling Tong ◽  
Junxiao Wu ◽  
Lin Tang ◽  
Pasquale Cinnella

2021 ◽  
Author(s):  
Stefan Heinz ◽  
Reza Mokhtarpoor ◽  
Michael K. Stoellinger

1990 ◽  
Vol 45 (1) ◽  
pp. 71-77 ◽  
Author(s):  
D. Guerillot ◽  
J. L. Rudkiewicz ◽  
C. Ravenne ◽  
G. Renard ◽  
A. Galli

2014 ◽  
Author(s):  
Donald L. Brown ◽  
Jun Li ◽  
Victor M. Calo ◽  
Mehdi Ghommem ◽  
Yalchin Efendiev

2018 ◽  
Vol 7 (4) ◽  
pp. 13-21
Author(s):  
Todd Backes ◽  
Charlene Takacs

There are a wide range of options for individuals to choose from in order to engage in aerobic exercise; from outdoor running to computer controlled and self-propelled treadmills. Recently, self-propelled treadmills have increased in popularity and provide an alternative to a motorized treadmill. Twenty subjects (10 men, 10 women) ranging in age from 19-23 with a mean of 20.4 ± 0.8 SD were participants in this study. The subjects visited the laboratory on three occasions. The purpose of the first visit was to familiarize the subject with the self-propelled treadmill (Woodway Curve 3.0). The second visit, subjects were instructed to run on the self-propelled treadmill for 3km at a self-determined pace. Speed data were collected directly from the self-propelled treadmill. The third visit used speed data collected during the self-propelled treadmill run to create an identically paced 3km run for the subjects to perform on a motorized treadmill (COSMED T150). During both the second and third visit, oxygen consumption (VO2) and respiratory exchange ratio (R) data were collected with COSMED’s Quark cardiopulmonary exercise testing (CPET) metabolic mixing chamber system. The VO2 mean value for the self-propelled treadmill (44.90 ± 1.65 SE ml/kg/min) was significantly greater than the motorized treadmill (34.38 ± 1.39 SE ml/kg/min). The mean R value for the self-propelled treadmill (0.91 ± 0.01 SE) was significantly greater than the motorized treadmill (0.86 ± 0.01 SE). Our study demonstrated that a 3km run on a self-propelled treadmill does elicit a greater physiological response than a 3km run at on a standard motorized treadmill. Self-propelled treadmills provide a mode of exercise that offers increased training loads and should be considered as an alternative to motorized treadmills.


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