TY - JOUR
T1 - The effect of solium caseinate concentration and processing on bubble sizes and their break-up and coalescence in turbulent, batch air/aqueous dispersions at atmospheric and elevated pressures
AU - Hu, Binjie
AU - Nienow, Alvin
AU - Pacek, Andrzej
PY - 2003/9/1
Y1 - 2003/9/1
N2 - The dispersion of air into aqueous solutions containing buffer and commercial sodium casemate at concentrations from 0.01 to 2% w/w has been studied under batch conditions. The air volume fraction, Phi, were 0.05, 0.1 and 0.2 and dispersion was achieved by means of Rushton turbine type impellers in a vessel of 0.15 m diameter. Bubble size distributions were measured by a stereo micro scope-video-computer technique as a function of time until equilibrium was reached after about 0.5 h following either a step increase or decrease in speed. The time to reach equilibrium was somewhat shorter for bubble break-up following a speed increase than for bubble coalescence following a speed decrease. However, somewhat surprisingly, at all concentration of Na-caseinate, coalescence occurred and at approximately the same rate. For the steady state conditions, the impact of agitation speed, air volume fraction and Na-caseinate concentration in terms of equilibrium surface tension could be accommodate by the equation: d(32)/D = 0.027 .(1 + 3.85 . Phi). We(-0.4) which is similar to equations found for batch liquid/liquid dispersions. Such an equation is not generally satisfactory for sparged gas-liquid systems. Some experiments were also conducted under pressure and these showed a decrease in d(32) at the same volume fraction of air as has also been found in bubble columns. (C) 2003 Elsevier Science B.V. All rights reserved.
AB - The dispersion of air into aqueous solutions containing buffer and commercial sodium casemate at concentrations from 0.01 to 2% w/w has been studied under batch conditions. The air volume fraction, Phi, were 0.05, 0.1 and 0.2 and dispersion was achieved by means of Rushton turbine type impellers in a vessel of 0.15 m diameter. Bubble size distributions were measured by a stereo micro scope-video-computer technique as a function of time until equilibrium was reached after about 0.5 h following either a step increase or decrease in speed. The time to reach equilibrium was somewhat shorter for bubble break-up following a speed increase than for bubble coalescence following a speed decrease. However, somewhat surprisingly, at all concentration of Na-caseinate, coalescence occurred and at approximately the same rate. For the steady state conditions, the impact of agitation speed, air volume fraction and Na-caseinate concentration in terms of equilibrium surface tension could be accommodate by the equation: d(32)/D = 0.027 .(1 + 3.85 . Phi). We(-0.4) which is similar to equations found for batch liquid/liquid dispersions. Such an equation is not generally satisfactory for sparged gas-liquid systems. Some experiments were also conducted under pressure and these showed a decrease in d(32) at the same volume fraction of air as has also been found in bubble columns. (C) 2003 Elsevier Science B.V. All rights reserved.
KW - pressure
KW - coalescence
KW - agitation
KW - sodium caseinate
KW - batch gas-liquid dispersions
UR - http://www.scopus.com/inward/record.url?scp=0042161859&partnerID=8YFLogxK
U2 - 10.1016/S0927-7765(03)00038-9
DO - 10.1016/S0927-7765(03)00038-9
M3 - Article
SN - 0927-7765
VL - 31
SP - 3
EP - 11
JO - Colloids and Surfaces B: Biointerfaces
JF - Colloids and Surfaces B: Biointerfaces
ER -