Determination of the effective interfacial area in rotating packed bed

2011 ◽  
Vol 168 (3) ◽  
pp. 1377-1382 ◽  
Author(s):  
Kuang Yang ◽  
Guangwen Chu ◽  
Haikui Zou ◽  
Baochang Sun ◽  
Lei Shao ◽  
...  
Keyword(s):  
Interfacial Area ◽  
Packed Bed ◽  
Rotating Packed Bed

Gas–Liquid Effective Interfacial Area in a Rotating Packed Bed

2012 ◽  
Vol 51 (50) ◽  
pp. 16320-16325 ◽  
Author(s):  
Yong Luo ◽  
Guang-Wen Chu ◽  
Hai-Kui Zou ◽  
Zhi-Qiang Zhao ◽  
Milorad P. Dudukovic ◽  
...  
Keyword(s):  
Interfacial Area ◽  
Packed Bed ◽  
Rotating Packed Bed

Systematic Approach to Determination of Maximum Achievable Capture Capacity via Leaching and Carbonation Processes for Alkaline Steelmaking Wastes in a Rotating Packed Bed

2013 ◽  
Vol 47 (23) ◽  
pp. 13677-13685 ◽  
Author(s):  
Shu-Yuan Pan ◽  
Pen-Chi Chiang ◽  
Yi-Hung Chen ◽  
Chun-Da Chen ◽  
Hsun-Yu Lin ◽  
...  
Keyword(s):  
Systematic Approach ◽  
Packed Bed ◽  
Rotating Packed Bed ◽  
Capture Capacity

A noninvasive X-ray technique for determination of liquid holdup in a rotating packed bed

2015 ◽  
Vol 138 ◽  
pp. 244-255 ◽  
Author(s):  
Yucheng Yang ◽  
Yang Xiang ◽  
Guangwen Chu ◽  
Haikui Zou ◽  
Yong Luo ◽  
...  
Keyword(s):  
Packed Bed ◽  
Liquid Holdup ◽  
X Ray ◽  
Rotating Packed Bed

Determination of specific interfacial areas in swirled two-phase flow

1983 ◽  
Vol 48 (3) ◽  
pp. 842-853
Author(s):  
Kurt Winkler ◽  
František Kaštánek ◽  
Jan Kratochvíl
Keyword(s):  
Interfacial Area ◽  
Liquid Volume ◽  
Upward Flow ◽  
Two Phase ◽  
Flow Rates ◽  
Mist Flow ◽  
Interfacial Areas ◽  
Correlation Parameters ◽  
Flow Components

Specific gas-liquid interfacial area in flow tubes 70 mm in diameter of the length 725 and 1 450 mm resp. containing various swirl bodies were measured for concurrent upward flow in the ranges of average gas (air) velocities 11 to 35 ms-1 and liquid flow rates 13 to 80 m3 m-2 h-1 using the method of CO2 absorption into NaOH solutions. Two different flow regimes were observed: slug flow swirled annular-mist flow. In the latter case the determination was carried out separately for the film and spray flow components, respectively. The obtained specific areas range between 500 to 20 000 m3 m-2. Correlation parameters are energy dissipation criteria, related to the geometrical reactor volume and to the static liquid volume in the reactor.

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