The appropriate feedforward compensator, $G_{ff}$, in the shown block diagram is

Step 1: Identify disturbance path to output.
The disturbance transfer function is:
\[
G_d(s) = \frac{2e^{-s}}{5s+1}
\]
Step 2: Identify the plant transfer function from input \(u\) to output \(y\).
The plant is:
\[
G_p(s) = \frac{3e^{-2s}}{8s+1}
\]
Step 3: For disturbance rejection via feedforward, output contribution must cancel.
To cancel the disturbance effect:
\[
G_{ff}(s)(-1)G_p(s) = -G_d(s)
\]
Thus:
\[
G_{ff}(s) = \frac{G_d(s)}{G_p(s)}
\]
Step 4: Substitute values.
\[
G_{ff}(s) = \frac{\frac{2e^{-s}}{5s+1}}{\frac{3e^{-2s}}{8s+1}}
\]
Simplify:
\[
G_{ff}(s)
= \frac{2}{5s+1} \cdot \frac{8s+1}{3} \cdot e^{\,s}
\]
But the feedforward block receives no delay compensation term because the diagram shows direct feedforward without delay matching, so:
\[
e^{s} \cdot e^{-2s} = e^{-s}
\]
Since the forward path already contains \(e^{-2s}\), the compensator must NOT add an exponential term (to avoid mismatch). Hence delays cancel properly, leaving only:
\[
G_{ff}(s)=\frac{2}{3}\frac{(8s+1)}{(5s+1)}
\]
Step 5: Final conclusion.
This matches option (A).
Final Answer: (A) \(\displaystyle \frac{2}{3}\frac{(8s+1)}{(5s+1)}\)
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:
