Ey. Kenig et al., MODELING OF REACTIVE ABSORPTION USING THE MAXWELL-STEFAN EQUATIONS, Industrial & engineering chemistry research, 36(10), 1997, pp. 4325-4334
The modeling and design of reactive absorption is based on a theoretic
al description of reaction and mass transport in multicomponent system
s. The multicomponent nature of these phenomena leads to complex proce
ss behavior due to the superposition of many driving forces-multicompo
nent diffusion, chemical interactions, convective flows, multicomponen
t thermodynamic interplay, etc. For this reason, an adequate theoretic
al description of the multicomponent reactive systems calls for the ap
plication of the Maxwell-Stefan equations and, further, for the use of
matrix coupled mass-transfer equations together with the relevant rea
ction kinetics. On this basis, a two-phase, gas-liquid system is consi
dered and a general model is developed for its design. Reactions in bo
th liquid and gas phases are taken into account, and both the film and
bulk reaction mechanisms are allowed for. The transport equation desc
ribing the film phenomena is solved analytically by using a linearizat
ion of the reaction term. The model is applied to the description of N
O, absorption. A comparison of the experimental and theoretical result
s demonstrated their good agreement.