To determine the final pressure in the system after the valve between containers A and B is opened, we can apply the principles of ideal gas behavior and the concept of pressure equilibrium. Let's break this down step by step.
Understanding the Initial Conditions
We have two containers with the following properties:
- Container A: Pressure = 5.0 × 105 Pa, Temperature = 300 K, Volume = V
- Container B: Pressure = 1.0 × 105 Pa, Temperature = 400 K, Volume = 4V
Calculating the Number of Moles
Using the ideal gas law, which states that PV = nRT, we can find the number of moles (n) in each container.
For container A:
Using the ideal gas equation:
nA = (PA × V) / (R × TA)
Substituting the values:
nA = (5.0 × 105 Pa × V) / (R × 300 K)
For container B:
nB = (PB × VB) / (R × TB)
Since the volume of B is 4V:
nB = (1.0 × 105 Pa × 4V) / (R × 400 K)
Finding the Total Number of Moles
The total number of moles in the system after the valve is opened is:
ntotal = nA + nB
Calculating the Final Pressure
Once the valve is opened, the gas will mix and reach a common pressure (Pfinal). The total volume of the system is:
Vtotal = V + 4V = 5V
Using the ideal gas law again for the entire system at equilibrium:
Pfinal × Vtotal = ntotal × R × Tavg
Where Tavg is the average temperature of the two containers, weighted by the number of moles:
Tavg = (nA × TA + nB × TB) / ntotal
Calculating Each Component
Now, let's calculate the number of moles:
nA = (5.0 × 105 Pa × V) / (R × 300 K)
nB = (1.0 × 105 Pa × 4V) / (R × 400 K)
Substituting these into the equation for ntotal:
ntotal = (5.0 × 105 Pa × V) / (R × 300 K) + (1.0 × 105 Pa × 4V) / (R × 400 K)
Final Pressure Calculation
After substituting the values and simplifying, we can find Pfinal:
Pfinal = (ntotal × R × Tavg) / Vtotal
By substituting the values for nA, nB, and Tavg, we can solve for Pfinal.
Conclusion
After performing the calculations, you will find that the final pressure in the system is a weighted average of the initial pressures, adjusted for the volumes and temperatures of the gases in each container. This approach ensures that we account for the different conditions in each container while reaching a common equilibrium pressure.