The following data is given for a ternary \(ABC\) gas mixture at 12 MPa and 308 K:
\(y_i\): mole fraction of component \(i\) in the gas mixture
\(\hat{\phi}_i\): fugacity coefficient of component \(i\) in the gas mixture at 12 MPa and 308 K
The fugacity of the gas mixture is _________ MPa (rounded off to 3 decimal places).
Step 1: Calculate the fugacity of each component. For Component \(A\): \(f_A = 0.55 \times 0.75 \times 12 = 4.95 \, {MPa}\) For Component \(B\): \(f_B = 0.20 \times 0.80 \times 12 = 1.92 \, {MPa}\) For Component \(C\): \(f_C = 0.25 \times 0.95 \times 12 = 2.85 \, {MPa}\)
Step 2: Sum the fugacities of all components to find the total fugacity of the mixture. \[ f = f_A + f_B + f_C = 4.95 + 1.92 + 2.85 = 9.72 \, {MPa}\]
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: \[ \frac{dy(t)}{dt} = \frac{t}{\tau^2} e^{-t/\tau} \] \[ \frac{d^2y(t)}{dt^2} = \frac{1}{\tau^2} \left(1 - \frac{t}{\tau}\right) e^{-t/\tau} \]