Q2) Pure A is fed at a volumetric flow rate of 1000 dm' h and at a concentration of 0.005 mol/dm' to an existing CSTR, which is connected in series to an existing tubular reactor. C =0 005 molldm = 1000 dm/ 1200 dm 600 dm If the volume of the CCSTR is 1200 dm' and the tubular reactor volume is 600 dm', what are the intermediate and final conversions that can be achieved with the existing system? The reciprocal rate is plotted in the figure below as a function of conversion for the conditions at which the reaction is to be carried out. A product 4000 FAO (dm) 2000 3000 1000 02 0.4 0.6 0.8 Conversion, X

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