Post

Created by @nathanedwards
 at November 1st 2023, 7:11:07 pm.

Question:

A gas undergoes a thermodynamic process described by the following steps:

  1. The gas is initially at a temperature of Ti=300KT_i = 300 \, \text{K} and a pressure of Pi=3atmP_i = 3 \, \text{atm}.
  2. The gas is compressed adiabatically to one-third of its initial volume.
  3. The gas is then cooled at constant volume until its temperature reaches Tf=100KT_f = 100 \, \text{K}.

Given that the molar specific heat capacity of the gas at constant volume is Cv=2.5cal/mol KC_v = 2.5 \, \text{cal/mol K}, and the molar gas constant is R=8.314J/mol KR = 8.314 \, \text{J/mol K}, determine:

a) The final pressure PfP_f of the gas after the adiabatic compression.

b) The work done on or by the gas during the adiabatic compression.

c) The heat transferred during the cooling process from step 2 to step 3.

Answer:

a) To find the final pressure PfP_f after the adiabatic compression, we can utilize the relation for an adiabatic process:

(PfPi)γ1=(ViVf)γ\begin{equation} \left(\frac{P_f}{P_i}\right)^{\gamma - 1} = \left(\frac{V_i}{V_f}\right)^{\gamma} \end{equation}

where ViV_i and VfV_f are the initial and final volumes, and γ\gamma is the heat capacity ratio which for a monoatomic ideal gas is γ=CpCv=52\gamma = \frac{C_p}{C_v} = \frac{5}{2}.

Since the gas is compressed to one-third of its initial volume, the final volume is Vf=13ViV_f = \frac{1}{3}V_i. Substituting these values into equation (1), we have:

(PfPi)521=(Vi13Vi)52\begin{equation} \left(\frac{P_f}{P_i}\right)^{\frac{5}{2} - 1} = \left(\frac{V_i}{\frac{1}{3}V_i}\right)^{\frac{5}{2}} \end{equation}

Simplifying equation (2), we get:

Pf=(131)523atm\begin{equation} P_f = \left(\frac{\frac{1}{3}}{1}\right)^{\frac{5}{2}} \cdot 3 \, \text{atm} \end{equation}
Pf=(13)523atm\begin{equation} P_f = \left(\frac{1}{3}\right)^{\frac{5}{2}} \cdot 3 \, \text{atm} \end{equation}

Evaluating the expression, we find:

Pf0.512atm\begin{equation} P_f \approx 0.512 \, \text{atm} \end{equation}

Therefore, the final pressure after the adiabatic compression is approximately 0.512atm0.512 \, \text{atm}.

b) The work done on or by the gas during an adiabatic process can be calculated using the following relation:

W=PiViPfVfγ1\begin{equation} W = \frac{P_i V_i - P_f V_f}{\gamma - 1} \end{equation}

We already know the values of PiP_i, ViV_i, PfP_f, and VfV_f. Substituting these values into equation (6), we have:

W=3atmVi0.512atm13Vi521\begin{equation} W = \frac{3 \, \text{atm} \cdot V_i - 0.512 \, \text{atm} \cdot \frac{1}{3}V_i}{\frac{5}{2} - 1} \end{equation}
W=3Vi13Vi32\begin{equation} W = \frac{3V_i - \frac{1}{3}V_i}{\frac{3}{2}} \end{equation}
W=89Vi\begin{equation} W = \frac{8}{9}V_i \end{equation}

Therefore, the work done on or by the gas during the adiabatic compression is 89Vi\frac{8}{9}V_i.

c) During the constant volume cooling from step 2 to step 3, the heat transferred can be calculated using the first law of thermodynamics:

Q=ΔU+W\begin{equation} Q = \Delta U + W \end{equation}

Since the process occurs at constant volume, there is no change in volume (ΔV=0\Delta V = 0), and therefore the work done by the gas is zero (W=0W = 0).

The change in internal energy ΔU\Delta U can be calculated using the equation:

ΔU=nCvΔT\begin{equation} \Delta U = nC_v\Delta T \end{equation}

where nn is the number of moles of the gas, CvC_v is the molar specific heat capacity at constant volume, and ΔT\Delta T is the change in temperature.

The number of moles nn can be calculated using the ideal gas equation:

PV=nRT\begin{equation} PV = nRT \end{equation}

Given that the initial pressure Pi=3atmP_i = 3 \, \text{atm} and the initial temperature Ti=300KT_i = 300 \, \text{K}, we can rearrange equation (12) to solve for nn:

n=PiViRTi\begin{equation} n = \frac{P_iV_i}{RT_i} \end{equation}

Substituting the known values into equation (13):

n=3atmVi(8.314J/mol K)(300K)\begin{equation} n = \frac{3 \, \text{atm} \cdot V_i}{(8.314 \, \text{J/mol K})\cdot(300 \, \text{K})} \end{equation}

Simplifying equation (14), we find:

n0.9067Viatm\begin{equation} n \approx \frac{0.9067V_i}{\text{atm}} \end{equation}

Now we can calculate ΔU\Delta U using equation (11), and since Q=ΔU+WQ = \Delta U + W, the heat transferred is equal to ΔU\Delta U:

Q=nCvΔT\begin{equation} Q = nC_v\Delta T \end{equation}
Q=(0.9067Viatm2.5cal/mol K)(100K300K)\begin{equation} Q = \left(\frac{0.9067V_i}{\text{atm}} \cdot 2.5 \, \text{cal/mol K}\right) (100 \, \text{K} - 300 \, \text{K}) \end{equation}

Converting the units from cal to J, we have:

Q=(0.9067Viatm2.5cal/mol K)(100K300K)(4.184J1cal)\begin{equation} Q = \left(\frac{0.9067V_i}{\text{atm}} \cdot 2.5 \, \text{cal/mol K}\right) (100 \, \text{K} - 300 \, \text{K}) \left(\frac{4.184 \, \text{J}}{1 \, \text{cal}}\right) \end{equation}
Q=2.109ViJ\begin{equation} Q = -2.109 \cdot V_i \, \text{J} \end{equation}

Therefore, the heat transferred during the cooling process from step 2 to step 3 is approximately 2.109ViJ-2.109 \cdot V_i \, \text{J}. Note that the negative sign indicates heat is transferred from the gas to the surroundings.