- Note Do Not Use Excel Please Show All The Necessary Solutions Process Please Answer From Letter D F Thank You 1 (39.75 KiB) Viewed 16 times
Note: Do not use excel please. Show all the necessary solutions/process. Please answer from letter d-f. Thank you...
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Note: Do not use excel please. Show all the necessary solutions/process. Please answer from letter d-f. Thank you...
Note: Do not use excel please. Show all the necessarysolutions/process. Please answer from letter d-f. Thank you...
The following exothermic reaction A → B+C was carried out adiabatically and the following data are recorded: X -TA mol dm³ min. 0 1.0 0.2 1.67 0.4 5.0 0.45 0.5 5.0 5.0 0.6 5.0 0.8 0.9 1.25 0.91 The entering molar flow rate of A was 300 mol/min. a) What are the PFR and CSTR volumes necessary to achieve 40% conversion? b) Over what range of conversions would the CSTR and PFR reactor volumes be identical? c) What is the maximum conversion that can be achieved in a 10.5 - dm³ CSTR? d) What conversion can be achieved if a 72 - dm³ PFR is allowed in series with a 24 dm³ CSTR? e) What conversion can be achieved if a 4- dm³ CSTR is followed in series with a 72 - dm³ PFR? f) Plot the conversion and rate of reaction as a function of PFR reactor volume up to a volume 100dm³.
The following exothermic reaction A → B+C was carried out adiabatically and the following data are recorded: X -TA mol dm³ min. 0 1.0 0.2 1.67 0.4 5.0 0.45 0.5 5.0 5.0 0.6 5.0 0.8 0.9 1.25 0.91 The entering molar flow rate of A was 300 mol/min. a) What are the PFR and CSTR volumes necessary to achieve 40% conversion? b) Over what range of conversions would the CSTR and PFR reactor volumes be identical? c) What is the maximum conversion that can be achieved in a 10.5 - dm³ CSTR? d) What conversion can be achieved if a 72 - dm³ PFR is allowed in series with a 24 dm³ CSTR? e) What conversion can be achieved if a 4- dm³ CSTR is followed in series with a 72 - dm³ PFR? f) Plot the conversion and rate of reaction as a function of PFR reactor volume up to a volume 100dm³.