Drop formation at nozzles submerged in quiescent continuous phase: an experimental study with TBP-dodecane and nitric acid system

2018 ◽  
Vol 29 (6) ◽  
Author(s):  
Amitava Roy ◽  
Mayur Darekar ◽  
K. K. Singh ◽  
K. T. Shenoy ◽  
R. B. Grover
2014 ◽  
Vol 32 (3) ◽  
pp. 281-300 ◽  
Author(s):  
Nirvik Sen ◽  
Mayur Darekar ◽  
K. K. Singh ◽  
S. Mukhopadhyay ◽  
K. T. Shenoy ◽  
...  

Author(s):  
Ф.В. Роньшин ◽  
Ю.А. Дементьев ◽  
Е.А. Чиннов

An experimental study of drop formation in narrow horizontal microchannels with rectangular cross section and a height from 50 to 150 micrometers was performed. It is shown that in these channels there is a new flow regime when drops moving along the microchannel, which are vertical liquid bridges. Three mechanisms of the formation of such drops are distinguished: the formation directly near the liquid nozzle, the separation of droplets from the liquid moving along the side walls of the channel, and due to the destruction of strongly deformed drops and horizontal liquid bridges. It was found that the deformation of drops increases with an increase in the Weber number. It is shown that when the first critical value of the Weber number is reached, the drops begin to deform, and when the second Weber number is reached, they break.


2001 ◽  
Vol 32 (7) ◽  
pp. 913-932 ◽  
Author(s):  
R Rudolf ◽  
A Vrtala ◽  
M Kulmala ◽  
T Vesala ◽  
Y Viisanen ◽  
...  

1994 ◽  
Vol 98 (23) ◽  
pp. 6030-6037 ◽  
Author(s):  
Istvan P. Nagy ◽  
Andrea Keresztessy ◽  
John A. Pojman ◽  
Gyorgy Bazsa ◽  
Zoltan Noszticzius

2012 ◽  
Vol 455-456 ◽  
pp. 503-506 ◽  
Author(s):  
Guo Bing Li ◽  
Hai Lin ◽  
Yan Li Ma ◽  
Yi Su

When precipitated silica was prepared from yellow phosphorus slag by the phosphoric acid leaching, the Fe content can not meet the quality requirements of the product. This article indicates the method of purifying precipitated silica with nitric acid solution, which may decrease the Fe content to about 0.02%. The purification optimum technical conditions are: the nitric acid concentration 8%, reaction time 2.0 hours, reaction temperature 343.15K, fluid solid ratio 4:1, stirring speed 300 rpm.


2006 ◽  
Vol 48 (3) ◽  
pp. 284-287
Author(s):  
M. N. Litvina ◽  
D. A. Malikov ◽  
T. A. Maryutina ◽  
Yu. M. Kulyako ◽  
B. F. Myasoedov

2015 ◽  
Vol 85 ◽  
pp. 1-10 ◽  
Author(s):  
Kinkar Mandal ◽  
Shekhar Kumar ◽  
V. Vijayakumar ◽  
U. Kamachi Mudali ◽  
A. Ravisankar ◽  
...  

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