23-Chem-A6 Process Dynamics and Control · December 2018
Question 2 of 8: State-Space Model — Transfer Function and Unit-Step Response
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Reference texts: D. E. Seborg, T. F. Edgar, D. A. Mellichamp & F. J. Doyle III, Process Dynamics and Control (4th ed., Wiley) — Laplace-domain modelling, linearisation, transfer functions, feedback stability, frequency response and IMC design; G. Stephanopoulos, Chemical Process Control: An Introduction to Theory and Practice (Prentice Hall) — Routh test, Nyquist criterion, dead-time systems and state-space models; D. R. Coughanowr & S. E. LeBlanc, Process Systems Analysis and Control (3rd ed., McGraw-Hill) — first-order tank/thermal dynamics, step/impulse response and block-diagram algebra. Standard control conventions (deviation variables; unity valve/sensor gains unless stated) are used throughout. This sitting is an open-book paper of eight problems of which any five constitute a complete exam; all eight are solved here.
Problem 2: State-Space Model — Transfer Function and Unit-Step Response (20%)
Find. (a) $Y(s)/U(s)$; (b) $y(t)$ for a unit step.
Problem 2: the response starts with negative slope ($\dot y(0^+)=-1.117$), dips below zero, then recovers to the positive steady value $0.585$ — the signature of the right-half-plane zero at $s=+2.817$.
Approach. Transform each state equation, solve the triangular system for $X_2=Y$, then invert the resulting third-order (with the $1/s$ input) rational function by partial fractions.
Transform the states. With zero initial conditions, $sX_1=-2.4048X_1+7U\Rightarrow X_1=\dfrac{7U}{s+2.4048}$, and $(s+2.2381)X_2=0.8333X_1-1.117U$.
(a) Transfer function. Substituting $X_1$: $(s+2.2381)X_2=\Big[\dfrac{0.8333\cdot7}{s+2.4048}-1.117\Big]U$. Since $0.8333\cdot7=5.8331$ and $5.8331-1.117\,(s+2.4048)=3.1469-1.117\,s$, $$\boxed{\frac{Y(s)}{U(s)}=\frac{3.1469-1.117\,s}{(s+2.4048)(s+2.2381)}.}$$ The steady-state gain is $3.1469/(2.4048\cdot2.2381)=0.585$; the numerator zero is at $s=+2.817$ (right half-plane), so an inverse response is expected.
Set up the step. For $U=1/s$, $$Y(s)=\frac{3.1469-1.117\,s}{s\,(s+2.4048)(s+2.2381)}=\frac{A}{s}+\frac{B}{s+2.4048}+\frac{C}{s+2.2381}.$$
Residues. $A=\dfrac{3.1469}{(2.4048)(2.2381)}=0.5847$; $B=\dfrac{3.1469-1.117(-2.4048)}{(-2.4048)(-2.4048+2.2381)}=\dfrac{5.8331}{0.4009}=14.55$; $C=\dfrac{3.1469-1.117(-2.2381)}{(-2.2381)(-2.2381+2.4048)}=\dfrac{5.6469}{-0.3731}=-15.14$. (Check: $A+B+C\approx0$, consistent with $y(0^+)=0$.)
(b) Time response. Inverting term by term, $$\boxed{y(t)=0.585+14.55\,e^{-2.4048\,t}-15.14\,e^{-2.2381\,t}.}$$ The two exponentials are large and nearly cancel; because the faster decays quicker, their difference is negative at first (initial slope $\dot y(0^+)=-1.117<0$), producing an inverse response before $y$ climbs to its final value $0.585$.