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( d ) What is the conversion of A in the first reactor? ( e ) If 9 9 % conversion of A is desired,
d What is the conversion of in the first reactor?
e If conversion of is desired, what reaction scheme and reactor
sizes should you use to maximize
f Suppose that and
What temperature would you recommend for a single CSTR with
a space time of min and an entering concentration of of
g If you could vary the pressure between and atm, what pressure
would you choose?
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