G1004 A Study on Pressure drop of Plug Flow of Coarse Particles

2005 ◽  
Vol 2005 (0) ◽  
pp. 329
Author(s):  
Kenji KOFU ◽  
Mitsuaki OCHI ◽  
Masahiro Takei
2003 ◽  
Vol 2003.38 (0) ◽  
pp. 20-21
Author(s):  
Shigemitu KAMATA ◽  
Mitsuaki OCHI ◽  
Masahiro TAKEI ◽  
Kenji KOFU

1982 ◽  
Vol 104 (2) ◽  
pp. 198-206 ◽  
Author(s):  
Y. Tsuji ◽  
Y. Morikawa

Plug flow of coarse particles was investigated experimentally in a horizontal pipe, in which a sub-pipe for secondary air injection was installed. Measurements were made about the plug motion, pressure drop, and transportation properties, and the roles of the main and sub-pipe air flow were clarified. The main air flow increases the number of plugs, while the sub-pipe air flow increases the plug velocity. The higher the main pipe air flow rate, the more regular the motion. The height of a stationary layer of deposited particles, which is built on the bottom of the main pipe, decreases with increasing the sub-pipe air flow rate. The pressure drop in the moving plug is quantitatively much smaller than that in the stationary packed bed of same particles.


2005 ◽  
Vol 2005 (0) ◽  
pp. 330
Author(s):  
Makoto TADOKORO ◽  
Mitsuaki OCHI ◽  
Masahiro TAKEI ◽  
Kenji KOFU

2004 ◽  
Vol 2004.2 (0) ◽  
pp. 427-428
Author(s):  
Daisuke YAMAMOTO ◽  
Mitsuaki OCHI ◽  
Masahiro TAKEI ◽  
Yoshihiro TANIGUCHI

2004 ◽  
Vol 2004 (0) ◽  
pp. 99
Author(s):  
Yoshihiro TANIGUCHI ◽  
Mitsuaki OCHI ◽  
Masahiro TAKEI ◽  
Kenji KOFU

Author(s):  
Namwon Kim ◽  
Michael C. Murphy ◽  
Steven A. Soper ◽  
Dimitris E. Nikitopoulos

Liquid-liquid segmented flows in microchannels fabricated on polymer test chips were investigated experimentally. Polymer test chips were prepared using hot embossing of polycarbonate (PC) sheets with micro-milled brass mold inserts. Three different configurations of microchannels were prepared with injection to test channels expansion ratios of 16, 4 and 2 and a fixed test channel geometry. Deionized water with blue food-coloring dye (1% v/v) was used as a dispersed fluid at flow rates (QD) between 0.5 and 60 μl/min. The carrier fluid was perfluorocarbon (FC 3283) with nonionic fluorous-soluble surfactant (Perfluorooctanol, 10% v/v) at flow rates (QC) between 3 and 25 μl/min. The two fluids were injected separately into the chips. Droplet and Plug flows with transient Irregular Segmented flows between two flow regimes were mainly observed in the test channels of the three different chips. Flow pattern maps and transitions between flow regimes were determined in terms of a fixed homogeneous carrier fluid volumetric flow ratio (βC) to compare the effect of the expansion ratios from the injection to the test channels. The droplet and plug regimes were shifted to higher carrier and lower dispersed fluid superficial velocities and the plug flow regime was broader with the lower expansion ratio channels. The transient irregular segmented flow was favored in the higher expansion channel ratio and the interval of transient irregular segmented flow between droplet and plug flow regimes were shorter for the low expansion channel ratios. This is evidence that flow regime maps in micro-channels are not universal and depend on the configuration part of the micro-injection system. The length of the dispersed segmented flows and the distance between consecutive droplets or plugs as a function of βC were determined by image processing of frames acquired via CCD camera with bright field illumination. The average length of the dispersed fluid was shown to scale approximately with βC to the −1.2 power. Velocities of the dispersed droplet and plug flows were measured using double-pulsed laser illumination and were found to be 1.25 ± 0.049 and 1.46 ± 0.077 times faster than the superficial velocity of the segmented flow respectively. Two-phase pressure drop measurements were also carried out for all flow regimes and associated trends were correlated with changes in flow topology. Comparisons of experimental pressure drop with the predictions for a modified Lockhart-Martinelli correlation were also made.


2011 ◽  
Vol 281 ◽  
pp. 179-182
Author(s):  
Hai Lu ◽  
Jun Yin ◽  
Yi Xing Yuan ◽  
Biao Wang ◽  
Hong Wei Chen ◽  
...  

Flow pattern and pressure drop in highly concentrated slurries transportation pipelines were discussed. The particles are settling, and tend to settle down to the bottom of pipes due to the action of gravity force forming different flow patterns which can be indicated by particle concentration profile. Three distinct flow patterns can be observed for different particle size distribution at different velocities: fully stratified, partially stratified and fully suspended flow patterns. As for pressure drop, it is well known that pressure drops in pipeline flows of slurries are strongly dependent on the flow pattern developed in a pipeline. Furthermore, fine particles suspended in water make the water more viscous, and increase the friction. In case of coarse particles, having larger volume, they have the tendency to contact with the pipe wall and with the other coarse particles more times, which increase the friction of flow. Meanwhile, coarse particles are lifted by the pressure difference generated as they rotate in the liquid preventing the coarse particles from settling down which results in less friction. The mixture of particles of different sizes is helpful to reduce pressure drop in pipeline flow slurries. Narrow grading particles tend to have high frictional losses, while broad grading particles have low frictional losses at high concentrations.


2016 ◽  
Vol 37 (4) ◽  
pp. 545-557 ◽  
Author(s):  
Bronisław Buczek ◽  
Piotr Zabierowski

Abstract Experiments on a confined fluidized bed system with various shapes of particles have been presented in the paper. Its influence on hydrodynamic properties in the whole range of gas velocity has been analysed. Relations allowing calculation of the Richardson-Zaki-type equation coefficients, including description of inter-particle void and gas pressure drop in such systems have been determined. Necessary condition for confined fluidization of non-spherical coarse particles has also been determined.


2005 ◽  
Vol 2005 (0) ◽  
pp. 328
Author(s):  
Akifumi OHNISHI ◽  
Mitsuaki OCHI ◽  
Masahiro TAKEI ◽  
Kenji KOFU

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