Step 1: Apply the phase rule.
The phase rule in thermodynamics is given by: \[ F = C - P + 2 \] where \(F\) is the number of degrees of freedom, \(C\) is the number of components, and \(P\) is the number of phases.
Step 2: Identify the components and phases.
For a ternary mixture at vapor-liquid-liquid equilibrium:
\(C = 3\) (ternary mixture implies three components),
\(P = 3\) (one vapor phase and two distinct liquid phases).
Step 3: Calculate the degrees of freedom.
Substituting the values into the phase rule: \[ F = 3 - 3 + 2 = 2 \] Thus, two independent intensive variables need to be specified to fully describe the system.
Is there any good show __________ television tonight? Select the most appropriate option to complete the above sentence.
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: \[ \frac{dy(t)}{dt} = \frac{t}{\tau^2} e^{-t/\tau} \] \[ \frac{d^2y(t)}{dt^2} = \frac{1}{\tau^2} \left(1 - \frac{t}{\tau}\right) e^{-t/\tau} \]