1. A rigid, sealed container holds of an ideal monatomic gas. The gas is initially in equilibrium at pressure and volume . The gas is taken through a two-step process from state 1 to state 3. In step 1, the gas is heated at constant volume from state 1 to state 2 until the pressure becomes . In step 2, the gas expands isothermally from state 2 to state 3 until the pressure becomes . A pressure-volume diagram for the process is shown in Figure 1.
Figure 1. Pressure–volume diagram for a two-step process: constant-volume heating from state 1 to state 2, followed by isothermal expansion from state 2 to state 3.
Figure 2. Microscopic model used to compare average molecular speed at state 1 and state 2 (constant volume).
Figure 3. Microscopic collision model used to compare pressure (force per unit area) at state 1 and state 2.
Complete the following tasks in Figures 2 and 3.
Indicate in Figure 2 whether the average molecular speed of the gas particles in state 2 is greater than, less than, or equal to the average molecular speed in state 1.
Indicate in Figure 3 whether the average force per unit area exerted on the container walls in state 2 is greater than, less than, or equal to that in state 1.
For the ideal monatomic gas, derive an expression for the total change in internal energy in terms of , , and the temperatures and . Then determine whether is positive, negative, or zero for the process shown.
Begin your derivation by writing a fundamental physics principle or an equation from the reference information.
Figure 4. Rigid gas container thermally connected to a large reservoir through a conducting slab (conduction only).
Calculate the magnitude of the rate of energy transfer by conduction through the slab at that instant. Then calculate the time required to raise the temperature of the gas from to if the conduction rate remains constant at the value you calculated and all transferred energy goes into increasing the internal energy of the gas. Finally, calculate the entropy change of the gas for heating from to at constant volume. The container is now brought into thermal contact with a large reservoir at constant temperature through a flat slab of material of thickness and cross-sectional area , as shown in Figure 4. The slab has thermal conductivity . At some instant, the gas temperature is . Assume the reservoir remains at and that energy is transferred only by conduction through the slab.
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