Analytical investigation of two different absorption modes: falling film and bubble types

The objectives of this paper are to analyze a combined heat and mass transf er for an ammonia-water absorption process, and to carry out the parametric analysis to evaluate the effects of important variables such as heat and m ass transfer areas on the absorption rate for two different absorption mode s - falling film and bubble modes. A plate heat exchanger with an offset st rip fin (OSF) in the coolant side was used to design the falling film and t he bubble absorber. It was found that the local absorption rate of the bubb le mode was always higher than that of the falling film model leading to ab out 48.7% smaller size of the heat exchanger than the falling film mode. Fo r the falling film absorption mode, mass transfer resistance was dominant i n the liquid flow while both heat and mass transfer resistances were consid erable in the vapor flow. For the bubble absorption mode, mass transfer res istance was dominant in the liquid flow while heat transfer resistance was dominant in the vapor region. Heat transfer coefficients had a more signifi cant effect on the heat exchanger size (absorption rate) in the falling fil m mode than in the bubble mode, while mass transfer coefficients had a more significant effect in the bubble mode than in the falling film mode. (C) 2 000 Elsevier Science Ltd and IIR. All rights reserved.