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The combination of reaction and distillation in one reactive distillation (RD) unit can lead to significant reduction of investment and operational cost. However, interactions between reactions and separation increase complexity and require a better understanding of the process. Whereas RD is intensively studied for years, only few works have been published on vapour¨Cliquid¨Cliquid (VLL) systems, thus our investigations focus on VLL reactive systems. Experimental investigations have already been published for the production of butyl acetate (Steinigeweg and Gmehling, 2002) or amyl acetate (Chiang et al., 2002) but, to the best of our knowledge, none for n-propyl acetate reactive distillation; thus, information about n-propyl acetate synthesis can hardly be found in literature. Investigations on reactive membrane separation have led Huang et al. (2005) to publish data on chemical equilibrium. Bart et al. (1996) have published a kinetic modelling of the n-propyl acetate synthesis catalysed by an ion exchange resin (Dowex) as well as Steinigeweg (2003) with the Amberlyst-15. Unfortunately, uncertainty remains on the chemical equilibrium constant value. Finally, no data about reactive distillation pilot-plant experiments is published.
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±¦MMC(½ð±Ò+20, ·­ÒëEPI+1): лл 2011-05-23 14:04:30
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