Experimental investigation of micro droplet formation mechanism at T-shaped junction

2019 ◽  
Vol 2019 (0) ◽  
pp. OS2-24
Author(s):  
Masamichi OISHI ◽  
Haruyuki KINOSHITA ◽  
Teruo FUJII ◽  
Marie OSHIMA
2013 ◽  
Vol 444 ◽  
pp. 345-358 ◽  
Author(s):  
M. Matos ◽  
M.A. Suárez ◽  
G. Gutiérrez ◽  
J. Coca ◽  
C. Pazos

2015 ◽  
Vol 93 (10) ◽  
pp. 1174-1183 ◽  
Author(s):  
Cheng-Han Wu ◽  
Weng-Sing Hwang

This study investigated the droplet formation mechanism using simulation analysis under various process conditions of ink-jet printing. Experimentally, the droplet shapes were cataloged in four types with the dwell time of the mono-polar waveform, and used to verify the reliability of the numerical model by finding consistency with the simulated modes of droplet formation. Conventional droplet formation depiction using pressure variation has not been comprehensive; as such, fluid propagating velocity was used to discuss the droplet formation mechanism in this study. Through the analysis of the fluid propagation velocity, a sufficient outward momentum of the fluid at the nozzle and a pulling force to pinch off the liquid thread were found to be essential for generating a single droplet. An insufficient pulling force would lead to undesired droplet shapes. A bipolar waveform can be used to enhance the outward momentum and the pulling force of the fluid, and the improvements in droplet formation were revealed in both the simulation and experiment. Results demonstrate that the analysis from the velocity variation is a useful and essential method when evaluating the droplet formation mechanism.


Energies ◽  
2021 ◽  
Vol 14 (5) ◽  
pp. 1341
Author(s):  
Li Lei ◽  
Yuting Zhao ◽  
Wukai Chen ◽  
Huiling Li ◽  
Xinyu Wang ◽  
...  

In this study, changes in the droplet formation mechanism and the law of droplet length in a two-phase liquid–liquid system in 400 × 400 μm standard T-junction microchannels were experimentally studied using a high-speed camera. The study investigated the effects of various dispersed phase viscosities, various continuous phase viscosities, and two-phase flow parameters on droplet length. Two basic flow patterns were observed: slug flow dominated by the squeezing mechanism, and droplet flow dominated by the shear mechanism. The dispersed phase viscosity had almost no effect on droplet length. However, the droplet length decreased with increasing continuous phase viscosity, increasing volume flow rate in the continuous phase, and the continuous-phase capillary number Cac. Droplet length also increased with increasing volume flow rate in the dispersed phase and with the volume flow rate ratio. Based on the droplet formation mechanism, a scaling law governing slug and droplet length was proposed and achieved a good fit with experimental data.


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