Note: 1-"Reactor design" should be understood as determining; the reactor type, value of the principle design parameter, dimensions, heat transfer properties (heat duty, heat transfer fluid temperature (its variation, if applicable), heat transfer area, etc.), properties of inlet-outlet streams (temperature, flow rate, composition), temperature and conversion gradients of the reactors (if applicable).

2- Additional assumptions can be made whenever necessary, however they should be discussed together with the results

As a chemical engineer you are asked to design alternative reactors for the production of P according to the following reaction:

A P

Feed stream contains 1 mol/min of A and 1.5 mol/min inert. You are expected to determine a target (final) conversion that is above 0.7

DATA: -DeltaH=18000 cal/mol Cp=250 cal/mol K Tmax=-95C Tmin=10C

design at least 2 different reactor systems, as one single and one consecutive flow reactors

- consider at least two different thermal operation conditions

-make use of appropriate software (MATLAB, Excel, etc)

show all your results schematically

- mention the software you used for different purposes clearly

discuss all your decisions and results

As a chemical eagineer you are asked to design alternative reactors for the production of P according to the following reaction: Feed stream contains 1 molimin of A and 1.5molmin inert. You are expected to determine a target (final) conversion that is above 0,7 and - design at least 2 differeat reactor systems, as one single and one consecutive flow reactors - consider at least two different thermal operation conditions - make use of appropriate sottware (MATLAB, Excel, stc) - show all your results schematically - mention the software you used for different purposes clearly - discuss all your decisions and results ote: 1. "Reacror design" should be understood as determining; the reactor type, value of the principle derign paramener, dimensions, heat transfer properties (heat duty, heat transfer fluid temperatioe (itr variation, if applicable), heat transfer area, etc.), properties of inlet-otellet streams (temperature, fows nate, compositione, remperature and conversion gradients of the reactors (if applicable). 2- Additional assumptions can be made wheneve necessary, however they should be discsssed together with the results DATA