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PLEASE PROVIDE COMPREHENSIVE FULL ANSWER TO ALL PARTS. Question 2 D L The second order reaction is taking place in 20 meters packed bed reactor of 1.5 in schedule 40 pipe that is packed with catalyst.A mixture of 17.4% of arbitrary gas A and 82.6% air is charged to a flow reactor in which A is oxidized at total pressure of 10 atm and constant temperature of 227C A+O2P The flow and packed bed information are as follows: m=325 Reaction rate constant=20 m/kmol-kgcar.h Entering volumetric flow rate=7.15m/h Catalyst pellet diameter=0.006m Solid catalyst density=1923 kg/m3 Pressure drop parameter:a=0.012 kg (a Setup the stoichiometric table for the reaction with calculated values for Oi (b Setup the algorithm of the reaction and derive the general design equation for the PBR. (c Calculate weight and void fraction of the catalyst bed to achieve a conversion of 70 % d Calculate the convcrsion achieved using the same bed in c but in the absence of pressure drop.

          PLEASE PROVIDE COMPREHENSIVE FULL ANSWER TO ALL PARTS.
Question 2 D L The second order reaction is taking place in 20 meters packed bed reactor of 1.5 in schedule 40 pipe that is packed with catalyst.A mixture of 17.4% of arbitrary gas A and 82.6% air is charged to a flow reactor in which A is oxidized at total pressure of 10 atm and constant temperature of 227C A+O2P
The flow and packed bed information are as follows: m=325 Reaction rate constant=20 m/kmol-kgcar.h Entering volumetric flow rate=7.15m/h Catalyst pellet diameter=0.006m Solid catalyst density=1923 kg/m3 Pressure drop parameter:a=0.012 kg (a Setup the stoichiometric table for the reaction with calculated values for Oi (b Setup the algorithm of the reaction and derive the general design equation for the PBR. (c Calculate weight and void fraction of the catalyst bed to achieve a conversion of 70 % d Calculate the convcrsion achieved using the same bed in c but in the absence of pressure drop.

please provide comprehensive full answer to all parts question 2 d l the second order reaction is taking place in 20 meters packed bed reactor of 15 in schedule 40 pipe that is packed with c 28026

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