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This is a sample exam from Process Modeling and System Theory (CHE 433), from year 2018.
Typology: Exams
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CHE 433 - Spring 2018 - Examination 2
This is an open book, open notes examination. Please read each problem carefully before attempting its solution. Show details of your effort. Good luck.
G(s) =
5(s − 2) (s + 1)(s + 2)(s + 3)
, G(s) =
Y (s) U(s)
Obtain the response of the output, y′(t), subject to a step change in u′(t) of magnitude 2, i.e., u′(t) = 2S(t). What is the ultimate change in y′(t) (t → ∞)? Equating dy′(t)/dt to zero, calculate t at which y′(t) will be minimum/maximum. Use the substitution z = exp(−t) to simplify the algebra for dy′(t)/dt = 0 [implies dy′(z)/dz = 0] and identify z and t where dy′(t)/dt = 0. Comparing the signs of extremum y′(t) and y′(∞), deduce that this extremum reflects an inverse response of the process.
d^2 y′ dt^2
dy′ dt
dy′ dt
with a being an arbitrary constant.
(a). Obtain the transfer function for the process, G(s). (b). Obtain expressions for the poles of G(s) - roots of the denominator of G(s). Show that the process is unstable for a ≤ 0. (c). For a > 0, deduce that G(s) can be put in the standard form for a second-order process. What are the values of K, τ , and ζ? At what value of a is the process critically damped? What are the ranges of a where the process is overdamped and underdamped?
(−rA) =
kCA (1 + aCA)
occurs in an isothermal, steady state CSTR, with v = v 0. For a = 5 L/mol, k = 0.5 min−^1 , CA 0 = 2 mol/L and τ = V /v 0 = 20 min, obtain the fractional conversion of A, X.
fig1fig 1). A first order reaction
A → B, r = kC
occurs in both reactors. The volumes of reaction mixture in both reactors are constant and equal (V ), the densities of all streams and the reaction mixtures in the two reactors are
constant and equal, and therefore, the volumetric flow rates F 0 , F 1 , F 2 and R are constant. Recognize that F 2 = F 0 , F 1 = (F 0 + R).
(a). Show that the mass balances for A for the two reactors are
dC 1 dt
C 1 , C 1 (0) = C 1 i
dC 2 dt
C 2 , C 2 (0) = C 2 i
(b). The following information is available: C 0 = 1 mol/L, R/F 0 = 0.4, F 0 /V = 1 min−^1 , k = 1 min−^1. Compute C 1 and C 2 at steady state. (c). The reactor system operating at steady state is subject to a perturbation in C 0. Derive the transfer function relating C 2 ′ to C 0 ′ using the parameter values in (b).
Figure 1: The system of two CSTRs with recycle. fig