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A sales representative of the company supplying the catalyst for unit x came along yesterday. The person said that their company has a new, more

A sales representative of the company supplying the catalyst for unit x came along yesterday. The person said that their company has a new, more active catalyst for the reaction.
A Money
The catalytically active material in the catalyst has not changed and the intrinsic rate constant for this first order reaction is k''=1.0.10-6ms-1 and the improved catalyst activity is claimed by a more efficient diffusion of the reagent to the active sites. Table P4 shows some of the characteristics of the catalyst, which is currently used, and the newly improved catalyst.
Table P4: Characteristics of current and newly developed catalysts.
\table[[,,Current catalyst,\table[[Newly developed],[catalyst]]],[dpeilet,mm,Diameter of pellet,10(spherical),10(spherical)],[particle,,Porosity of pellet,0.4,0.5],[dpare,nm,Pore diameter,40,75],[S,m2g,Specific surface area,16.7,13.3],[catalyst,gcm3,Density of catalyst,2.4,2.0]]
a) Determine the effectiveness factor for the currently used catalyst knowing that the effective diffusivity of A in the pores of the currently catalyst is 8.8.10-7m2s, and comment on the influence of mass transfer on the reaction.
b) Estimate the effective diffusivity of A in the newly developed catalyst assuming that Knudsen diffusion is the dominant transport mechanism assuming that the tortuosity and the constriction factor remain the same.
c) Estimate the effectiveness factor over the newly developed catalyst, and comment on the improved mass transfer.
d) Currently, a conversion of A of 75% using 1250kg of catalyst in an isothermal packed bed reactor is achieved. What conversion can be expected with the same feed and having 1000kg of the new catalysts?
(7)
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