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Shrinking core reaction modulus

From the above discussion we see that the shrinking-core reaction modulus (Tg provides a simple but general criterion for the relative importance of chemical reaction and diffusion. The effect of is shown in Fig. 3.10 for... [Pg.87]

Tg shrinking-core reaction modulus for the grain defined by Eq. [Pg.173]

The shrinking core reaction mode is not necessarily limited to non-porous unreacted solids. With a fast reaction in a porous solid, diffusion into the core and chemical reaction occur in parallel. The mechanism of the process is very similar to the mechanism of the catalysed gas-solid reactions where the Thiele modulus is large, the effectiveness factor is small and the reaction is confined to a thin zone (Section 3.3.1). This combination of reaction with core diffusion gives rise to a reaction zone which, although not infinitely thin but diffuse, nevertheless advances into the core at a steady rate. [Pg.184]

Several models that describe gas-solid noncatalytic reactions are summarized in Table 7-7. The first two, the sharp interface and volume reaction models, are pseudo-homogeneous, form part of the class of shrinking core models, and can be treated by using the Thiele modulus and effectiveness factor concept. The last three are heterogeneous models. [Pg.23]


See other pages where Shrinking core reaction modulus is mentioned: [Pg.77]    [Pg.106]    [Pg.77]    [Pg.106]    [Pg.778]    [Pg.244]   
See also in sourсe #XX -- [ Pg.77 , Pg.87 , Pg.106 , Pg.173 ]




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