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Pseudo-chemical potential definition

In order to exemplify the potential of micro-channel reactors for thermal control, consider the oxidation of citraconic anhydride, which, for a specific catalyst material, has a pseudo-homogeneous reaction rate of 1.62 s at a temperature of 300 °C, corresponding to a reaction time-scale of 0.61 s. In a micro channel of 300 pm diameter filled with a mixture composed of N2/02/anhydride (79.9 20 0.1), the characteristic time-scale for heat exchange is 1.4 lO" s. In spite of an adiabatic temperature rise of 60 K related to such a reaction, the temperature increases by less than 0.5 K in the micro channel. Examples such as this show that micro reactors allow one to define temperature conditions very precisely due to fast removal and, in the case of endothermic reactions, addition of heat. On the one hand, this results in an increase in process safety, as discussed above. On the other hand, it allows a better definition of reaction conditions than with macroscopic equipment, thus allowing for a higher selectivity in chemical processes. [Pg.39]


See other pages where Pseudo-chemical potential definition is mentioned: [Pg.286]    [Pg.84]    [Pg.199]    [Pg.87]    [Pg.241]    [Pg.248]    [Pg.70]    [Pg.7]    [Pg.3]   
See also in sourсe #XX -- [ Pg.259 , Pg.260 , Pg.261 , Pg.262 , Pg.263 , Pg.264 , Pg.265 ]




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