An Experimental Study of Local Mass Transfer Characteristics on Inclined Flat Plate

2011 ◽  
Vol 35 (12) ◽  
pp. 1335-1341
Author(s):  
Seong-Yeon Yoo ◽  
Woo-Sik Jo ◽  
Woong-Sun Cho
Keyword(s):  
Mass Transfer ◽  
Experimental Study ◽  
Flat Plate ◽  
Local Mass ◽  
Transfer Characteristics ◽  
Local Mass Transfer

Experimental Study on Local Mass Transfer in a Simplified Bifurcation Model: Potential Role in Atherosclerosis

2004 ◽  
Vol 32 (11) ◽  
pp. 1504-1518 ◽  
Author(s):  
Nader Mahinpey ◽  
Richard Leask ◽  
Matadial Ojha ◽  
K. Wayne Johnston ◽  
Olev Trass
Keyword(s):  
Mass Transfer ◽  
Experimental Study ◽  
Potential Role ◽  
Model Potential ◽  
Local Mass ◽  
Local Mass Transfer

scholarly journals The flow and mass transfer characteristics of concentric gas-liquid flow in an advanced static mixer

2020 ◽  
pp. 24-24
Author(s):  
Huibo Meng ◽  
Zhonggen Li ◽  
Yanfang Yu ◽  
Mengqi Han ◽  
Shuning Song ◽  
...  
Keyword(s):  
Mass Transfer ◽  
Liquid Flow ◽  
Operating Conditions ◽  
Static Mixer ◽  
Transfer Coefficients ◽  
Mass Transfer Coefficients ◽  
Local Mass ◽  
Transfer Characteristics ◽  
Local Mass Transfer ◽  
Gas Liquid Flow

The fluid dynamic and mass transfer characteristics of concentric upward gas-liquid flow were studied in the industrial static mixer with four equally spaced helical inserts (FKSM). The numerical simulations of gas volume fraction in Kenics mixer had a good agreement with the numerical and experimental results provided by Rabha et al. The characteristics of radial gas void fraction and local mass transfer coefficients in the FKSM were evaluated under different operating conditions. The velocity profiles of concentric air phase accelerated by the bubble forces firstly became sharp and narrow until z/l=-3.27 and then slowly decreased and stabilized at z/l=-1.5 before entering the first mixing element. Some extra unimodal profile of radial gas holdup gradually generated near the rectangle cross sections of mixing elements. The ?G gradually enlarged from r/R=0.2 to r/R=0.55 and then weakened from r/R=0.65 to r/R=0.874. The air void fractions in the bulk flow region decreased with the increasing initial uniform bubble diameter. The inlet effect of first leading edge enhanced the air phase dispersion and local mass transfer coefficients sharply increased from 2.04 to 3.69 times of that in the inlet. The local mass transfer coefficients in each mixing group had unimodal profiles.

Hydrodynamics and local mass transfer characteristics of gas-liquid ejectors

1993 ◽  
Vol 53 (1) ◽  
pp. 67-73 ◽  
Author(s):  
P.H.M.R. Cramers ◽  
L. Smit ◽  
G.M. Leuteritz ◽  
L.L. van Dierendonck ◽  
A.A.C.M. Beenackers
Keyword(s):  
Mass Transfer ◽  
Local Mass ◽  
Transfer Characteristics ◽  
Local Mass Transfer
Sign in / Sign up

Export Citation Format

Share Document