The third-order gas-phase reaction | ||
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is to be carried out in a nonideal reactor whose macromixing
can be characterized by the RTD in Figure 13-9(a). The space-times corresponding
to the figure areCSTR
= 50 s andPFR
= 50 s. The specific reaction rate is k = 500 dm
6/mol2s
and the entering concentration of A is 0.02 mol/dm3.
Calculate the conversion assuming that the micromixing is described by:
(a) Figure E13-3.1. (b) Figure E13-3.2. (c) Three reactors in series: a PFR ( = 25 s) followed by a CSTR ( = 50 s) and then a PFR ( = 25 s). (d) The complete segregation and maximum mixedness models. |
[2nd Ed. P13-10]