Bb. Breman et al., THE GAS-LIQUID MASS-TRANSFER COEFFICIENT (K(L)A) IN THE GAS-LIQUID MULTISTAGE AGITATED CONTACTOR (MAC), Chemical engineering research & design, 74(A8), 1996, pp. 872-881
Data on the volumetric liquid-side gas-liquid mass transfer coefficien
t, k(L)a, in a Multi-stage Agitated Contractor (MAC) are reported for
three gas-liquid systems (air-water, helium-n-octane, and air-Monoethy
lene Glycol (MEG)). k(L)a (s(-1)) was determined using a dynamic metho
d with moderately soluble gaseous tracers (acetylene for water and MEG
and methane for n-octane). The observed response curves could be desc
ribed accurately by coupling the single phase residence time distribut
ion models for gas and liquid phase (Breman et al., (1,2)), via interf
acial gas-liquid mass transfer. All k,a data could be correlated with
an average relative deviation of 11.3% by a combination of Calderbanks
' relation(3) for k(L) (m s(-1)) and a modified type of Calderbanks' r
elation(3) for the interfacial area, a (m(-1)), which takes a combined
effect of the superficial gas velocity (u(G)) and the liquid viscosit
y (eta(L)) on a into account: a = 51.1(P/V)(0.286) sigma(-0.19)(u(G)/v
(b))((0.127+21.1 eta L)) with g = acceleration of gravity (= 9.81 m(2)
s(-1)), P/V = volumetric power input (W/m(-3)), v(b) = bubble rise ve
locity (m s(-1)) and the experimental conditions ranging from: superfi
cial gas velocity u(G) = 0.01-0.09 m s(-1), stirring speed (N) = 10-36
.7 rev s(-1), eta(L) = 0.00041-0.021 N m(-2) s, surface tension (sigma
) = 0.02-0.073 N m(-1), liquid density (rho(L)) = 684-1113 kg m(-3), g
as density (rho(G)) = 0.16-1.205 kg m(-3) and liquid diffusion coeffic
ient (L-L) = 1.3 x 10(-10)-3.5 x 10(-9) m(2) s(-1). The overall influe
nce of u(G) on k(L)a in this relation is such that k(L)a is hardly aff
ected by u(G) both for water and n-octane, whereas, in contrast, k(L)a
is predicted to increase significantly with increasing u(G) for the m
ore viscous monoethylene glycol, The general applicability of the prop
osed relation for a has to be confirmed by measurements for other liqu
ids and by measurements on a larger scale.