
Step 1: Loop reduction up to the point where \(d_2\) enters
Let \(G_1(s)=\dfrac{1}{0.1s+1}\) and \(G_2(s)=\dfrac{1}{s+1}\). From the diagram, the signal entering the \(d_2\)-summer comes from a unity gain followed by a controller of gain \(10\), and there is an outer unity feedback from \(y\) to the first summer (error \(=y_{\text{set}}-y\)). With \(y_{\text{set}}=0\) (for disturbance transfer) the path from \(y\) back to the \(d_2\)-summer through the controller forms a feedback around the plant. The equivalent forward block from the \(d_2\)-summer to \(y\) is \(G_1G_2\) with a feedback path of gain \(10\).
Step 2: Closed-loop due to the controller feedback
Writing the closed-loop relation at the \(d_2\)-injection node (call its signal \(u\)): \[ y \;=\; G_1G_2\big(d_2 - 10\,y\big) \quad\Rightarrow\quad y\big(1+10G_1G_2\big)=G_1G_2\,d_2 . \] Hence \[ \frac{y}{d_2}=\frac{G_1G_2}{1+10G_1G_2} = \frac{1}{(0.1s+1)(s+1)+10}. \]
Step 3: Rearrangement to the factored form
\[ (0.1s+1)(s+1)+10 =0.1s^2+1.1s+11 = (0.1s+1)(11s+21). \] Therefore \[ G_{d2}(s)=\frac{1}{(11s+21)(0.1s+1)}. \] This matches option (A).


Consider a process with transfer function: \[ G_p = \frac{2e^{-s}}{(5s + 1)^2} \] A first-order plus dead time (FOPDT) model is to be fitted to the unit step process reaction curve (PRC) by applying the maximum slope method. Let \( \tau_m \) and \( \theta_m \) denote the time constant and dead time, respectively, of the fitted FOPDT model. The value of \( \frac{\tau_m}{\theta_m} \) is __________ (rounded off to 2 decimal places).
Given: For \( G = \frac{1}{(\tau s + 1)^2} \), the unit step output response is: \[ y(t) = 1 - \left(1 + \frac{t}{\tau}\right)e^{-t/\tau} \] The first and second derivatives of \( y(t) \) are: \[ \frac{dy(t)}{dt} = \frac{t}{\tau^2} e^{-t/\tau} \] \[ \frac{d^2y(t)}{dt^2} = \frac{1}{\tau^2} \left(1 - \frac{t}{\tau}\right) e^{-t/\tau} \]
Choose the transfer function that best fits the output response to a unit step input change shown in the figure:

An electrical wire of 2 mm diameter and 5 m length is insulated with a plastic layer of thickness 2 mm and thermal conductivity \( k = 0.1 \) W/(m·K). It is exposed to ambient air at 30°C. For a current of 5 A, the potential drop across the wire is 2 V. The air-side heat transfer coefficient is 20 W/(m²·K). Neglecting the thermal resistance of the wire, the steady-state temperature at the wire-insulation interface __________°C (rounded off to 1 decimal place).

GIVEN:
Kinematic viscosity: \( \nu = 1.0 \times 10^{-6} \, {m}^2/{s} \)
Prandtl number: \( {Pr} = 7.01 \)
Velocity boundary layer thickness: \[ \delta_H = \frac{4.91 x}{\sqrt{x \nu}} \]
The first-order irreversible liquid phase reaction \(A \to B\) occurs inside a constant volume \(V\) isothermal CSTR with the initial steady-state conditions shown in the figure. The gain, in kmol/m³·h, of the transfer function relating the reactor effluent \(A\) concentration \(c_A\) to the inlet flow rate \(F\) is:
