A second-order reaction is to be carried out in a real reactor which gives the following outlet concentration for a step input.
For 0 ≤ t<10 min then CT = 10
For t ≥10 min then CT= 5+10 (l−0 2(t-10))
(a) What model do you propose and what are your model parameters, a and P?
(b) What conversion can be expected in the real reactor?
(c) How would your model change and conversion change if your outlet tracer concentration was
For t ≤ 10 min, then CT = 0
For t ≥ 10 min, then CT= 5+ 10 (1−e-0.2(t−10))
Υ0= 1 dm2/min, k = 0.1 dm3/mol min, CA0 = 1.25 mol/dm3
We need at least 10 more requests to produce the solution.
0 / 10 have requested this problem solution
The more requests, the faster the answer.