You have two CSTRs and two PFRs, each with a volume of 1.0 m3 . Use the following processed data to calculate the conversion for each of the reactors in the following arrangements

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(a) Two CSTRs in series. (b) Two PFRs in series. (c) A PFR followed by a CSTR. (d) A CSTR followed by a PFR.

\begin{tabular}{|c|ccccccc|} \hlineX & 0.0 & 0.1 & 0.2 & 0.4 & 0.6 & 0.7 & 0.8 \\ \hlinerA(m3smol) & 0.45 & 0.37 & 0.30 & 0.195 & 0.113 & 0.079 & 0.05 \\ \hline(1/rA)(molm3s) & 2.22 & 2.70 & 3.33 & 5.13 & 8.85 & 12.7 & 20 \\ \hline(FAd(rA)(m3) & 0.89 & 1.08 & 1.33 & 2.05 & 3.54 & 5.06 & 8.0 \\ \hline \end{tabular}