The reactive process AP described by the following kinetic expression: kgmol TAK K = 0.015 Sm³ has to carried out in a c

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The reactive process AP described by the following kinetic expression: kgmol TAK K = 0.015 Sm³ has to carried out in a c

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The Reactive Process Ap Described By The Following Kinetic Expression Kgmol Tak K 0 015 Sm Has To Carried Out In A C 1
The Reactive Process Ap Described By The Following Kinetic Expression Kgmol Tak K 0 015 Sm Has To Carried Out In A C 1 (28.4 KiB) Viewed 42 times
The Reactive Process Ap Described By The Following Kinetic Expression Kgmol Tak K 0 015 Sm Has To Carried Out In A C 2
The Reactive Process Ap Described By The Following Kinetic Expression Kgmol Tak K 0 015 Sm Has To Carried Out In A C 2 (18.03 KiB) Viewed 42 times
The reactive process AP described by the following kinetic expression: kgmol TAK K = 0.015 Sm³ has to carried out in a continuous stirred reactor with a volume of 1m³ having an available stream containing only compound A (CA0-1kgmol/m³. Q-Im³/min). The geometric characteristics of the reactor are shown in the figure. Determine the maximum achievable conversion and the optimal operating conditions of the agitation system in terms of the number of rotations of the impeller. The physico-chemical characteristics of the stream are: density 1000kg/m³, viscosity 0.1 Pa s and molecular diffusivity 4.5x108 m²/s.
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