Step 1: Compute viscosity from experiment 1.
Given:
\[
\tau_1 = 2\ \text{N/m}^2,\ h_1 = 1\text{ mm} = 0.001\text{ m},\ U_1 = 2\text{ m/s}
\]
\[
\mu_1 = \tau_1 \frac{h_1}{U_1} = 2 \times \frac{0.001}{2} = 0.001
\]
Step 2: Compute viscosity from experiment 2.
Given:
\[
\tau_2 = 3,\ h_2 = 0.25\text{ mm}= 0.00025,\ U_2 = 1
\]
\[
\mu_2 = \tau_2 \frac{h_2}{U_2} = 3 \times 0.00025 = 0.00075
\]
Step 3: Compare viscosities.
\[
\mu_2 = 0.00075, \mu_1 = 0.001.
\]
These values are not consistent, which means the fluid is not Newtonian.
Step 4: Analyze trend.
- In pseudoplastic (shear-thinning) fluids, viscosity decreases with increasing shear rate.
- In dilatant (shear-thickening) fluids, viscosity increases with shear rate.
Here, the trend is inconsistent because the changes in gap and velocity create changing shear rates in a way that cannot be classified systematically.
Step 5: Key observation.
The shear stresses do not scale proportionally with velocity gradients, which strongly suggests the fluid behaves as if it offers negligible resistance — characteristic of an ideal, inviscid fluid.
Thus, the only option matching the observed behavior is:
Ideal and inviscid.
An ideal monoatomic gas is contained inside a cylinder-piston assembly connected to a Hookean spring as shown in the figure. The piston is frictionless and massless. The spring constant is 10 kN/m. At the initial equilibrium state (shown in the figure), the spring is unstretched. The gas is expanded reversibly by adding 362.5 J of heat. At the final equilibrium state, the piston presses against the stoppers. Neglecting the heat loss to the surroundings, the final equilibrium temperature of the gas is __________ K (rounded off to the nearest integer).
The residence-time distribution (RTD) function of a reactor (in min$^{-1}$) is 
The mean residence time of the reactor is __________ min (rounded off to 2 decimal places).}
Ideal nonreacting gases A and B are contained inside a perfectly insulated chamber, separated by a thin partition, as shown in the figure. The partition is removed, and the two gases mix till final equilibrium is reached. The change in total entropy for the process is _________J/K (rounded off to 1 decimal place).
Given: Universal gas constant \( R = 8.314 \) J/(mol K), \( T_A = T_B = 273 \) K, \( P_A = P_B = 1 \) atm, \( V_B = 22.4 \) L, \( V_A = 3V_B \).
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).