Step 1: Open-loop transfer function with proportional controller gain \(K_c\): \[ G(s) = K_c \cdot \frac{0.25(1-s)}{s(2s+1)}. \]
Step 2: Closed-loop characteristic equation: \[ 1+G(s)=0 \;\;\Rightarrow\;\; 1+ \frac{0.25K_c(1-s)}{s(2s+1)}=0. \] Multiply through: \[ s(2s+1) + 0.25K_c(1-s) = 0. \]
Step 3: Simplify: \[ 2s^2 + s + 0.25K_c -0.25K_c s = 0, \] \[ 2s^2 + \big(1-0.25K_c\big)s + 0.25K_c=0. \]
Step 4: For decaying oscillations, the system must be underdamped (complex roots with negative real parts). Condition: \[ \Delta = b^2 - 4ac < 0, \] where \(a=2,\; b=(1-0.25K_c),\; c=0.25K_c\). \[ \Delta=(1-0.25K_c)^2 - 2K_c. \]
Step 5: Test given options:
Final Answer: \[ \boxed{K_c = 2} \]



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: \[ \frac{dy(t)}{dt} = \frac{t}{\tau^2} e^{-t/\tau} \] \[ \frac{d^2y(t)}{dt^2} = \frac{1}{\tau^2} \left(1 - \frac{t}{\tau}\right) e^{-t/\tau} \]
Methanol is produced by the reversible, gas-phase hydrogenation of carbon monoxide: \[ {CO} + 2{H}_2 \rightleftharpoons {CH}_3{OH} \] CO and H$_2$ are charged to a reactor, and the reaction proceeds to equilibrium at 453 K and 2 atm. The reaction equilibrium constant, which depends only on the temperature, is 1.68 at the reaction conditions. The mole fraction of H$_2$ in the product is 0.4. Assuming ideal gas behavior, the mole fraction of methanol in the product is ____________ (rounded off to 2 decimal places).