You have two CSTRs and two PFRs each with a volume of 1.6 m3. Use Figure 2-2 to calculate...

You have two CSTRs and two PFRs each with a volume of 1.6 m3. Use Figure 2-2 to calculate the conversion for each of the reactors in the following arrangements.

(a) Two CSTRs in series.

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(b) Two PFRs in series.

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(c) Two CSTRs in parallel with the feed, FA0, divided equally between the two reactors.

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(d) Two PFRs in parallel with the feed divided equally between the two reactors.

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(e) A CSTR and a PFR in parallel with the flow equally divided. Also calculate the overall conversion, Xov

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(f) A PFR followed by a CSTR.

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(g) A CSTR followed by a PFR.

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(h) A PFR followed by two CSTRs. Is this arrangement a good one or is there a better one?