Solveeit Logo

Question

Question: Heat leaks into a vessel, containing one mole of an ideal monoatomic gas at a constant rate of $\fra...

Heat leaks into a vessel, containing one mole of an ideal monoatomic gas at a constant rate of R4s1\frac{R}{4} s^{-1} where R is universal gas constant. It is observed that the gas expands at a constant rate dVdt=V0400(second)\frac{dV}{dt} = \frac{V_0}{400 (second)} where V0V_0 is initial volume. The initial temperature is given by T0=40KT_0 = 40 K. What will be final temperature of gas at time t = 400 s.

A

40 K

B

80 K

C

200 K

D

260 K

Answer

80 K

Explanation

Solution

The problem describes a thermodynamic process for one mole of an ideal monoatomic gas. We are given:

  1. Amount of gas: n=1n = 1 mole.
  2. Gas type: Ideal monoatomic.
  3. Rate of heat leak into the vessel: dQdt=R4\frac{dQ}{dt} = \frac{R}{4} (assuming RR is the universal gas constant and the rate is in Watts, i.e., J/s).
  4. Rate of volume expansion: dVdt=V0400\frac{dV}{dt} = \frac{V_0}{400} (assuming V0V_0 is the initial volume and the rate is in m3/sm^3/s).
  5. Initial temperature: T0=40T_0 = 40 K.
  6. Initial volume: V0V_0.
  7. Time duration: t=400t = 400 s.

We use the First Law of Thermodynamics: ΔQ=ΔU+ΔW\Delta Q = \Delta U + \Delta W. Differentiating with respect to time, we get: dQdt=dUdt+dWdt\frac{dQ}{dt} = \frac{dU}{dt} + \frac{dW}{dt}

For an ideal monoatomic gas, the internal energy U=32nRTU = \frac{3}{2} nRT. So, the rate of change of internal energy is: dUdt=32nRdTdt\frac{dU}{dt} = \frac{3}{2} nR \frac{dT}{dt} Since n=1n=1, dUdt=32RdTdt\frac{dU}{dt} = \frac{3}{2} R \frac{dT}{dt}.

The rate of work done by the gas is dWdt=PdVdt\frac{dW}{dt} = P \frac{dV}{dt}. Using the ideal gas law, PV=nRTPV = nRT, we have P=nRTVP = \frac{nRT}{V}. Substituting this into the work rate equation: dWdt=nRTVdVdt\frac{dW}{dt} = \frac{nRT}{V} \frac{dV}{dt} Since n=1n=1, dWdt=RTVdVdt\frac{dW}{dt} = \frac{RT}{V} \frac{dV}{dt}.

Now, substitute these into the First Law equation: R4=32RdTdt+RTVdVdt\frac{R}{4} = \frac{3}{2} R \frac{dT}{dt} + \frac{RT}{V} \frac{dV}{dt}

We can divide the entire equation by RR: 14=32dTdt+TVdVdt\frac{1}{4} = \frac{3}{2} \frac{dT}{dt} + \frac{T}{V} \frac{dV}{dt}

We are given that dVdt=V0400\frac{dV}{dt} = \frac{V_0}{400}, which is a constant rate. Integrating this to find the volume V(t)V(t) at any time tt: V(t)=V0+V0400t=V0(1+t400)V(t) = V_0 + \frac{V_0}{400} t = V_0 \left(1 + \frac{t}{400}\right)

Substitute V(t)V(t) into the energy equation: 14=32dTdt+TV0(1+t400)(V0400)\frac{1}{4} = \frac{3}{2} \frac{dT}{dt} + \frac{T}{V_0 \left(1 + \frac{t}{400}\right)} \left(\frac{V_0}{400}\right) 14=32dTdt+T400+t400(1400)\frac{1}{4} = \frac{3}{2} \frac{dT}{dt} + \frac{T}{\frac{400+t}{400}} \left(\frac{1}{400}\right) 14=32dTdt+T400+t\frac{1}{4} = \frac{3}{2} \frac{dT}{dt} + \frac{T}{400+t}

Rearranging this first-order linear differential equation: dTdt+23(400+t)T=16\frac{dT}{dt} + \frac{2}{3(400+t)} T = \frac{1}{6}

The integrating factor is (400+t)2/3(400+t)^{2/3}. Multiplying by the IF: ddt[T(400+t)2/3]=16(400+t)2/3\frac{d}{dt} \left[ T (400+t)^{2/3} \right] = \frac{1}{6} (400+t)^{2/3}

Integrating both sides: T(400+t)2/3=110(400+t)5/3+CT (400+t)^{2/3} = \frac{1}{10} (400+t)^{5/3} + C

Using the initial condition T(0)=40T(0) = 40 K: 40(400)2/3=110(400)5/3+C    C=040 (400)^{2/3} = \frac{1}{10} (400)^{5/3} + C \implies C = 0.

So, T(t)=110(400+t)T(t) = \frac{1}{10} (400+t). At t=400t = 400 s: T(400)=110(400+400)=80010=80T(400) = \frac{1}{10} (400 + 400) = \frac{800}{10} = 80 K.

This process is isobaric because V(t)=V0400+t400V(t) = V_0 \frac{400+t}{400} and T(t)=400+t10T(t) = \frac{400+t}{10}, which implies VTV \propto T. For an isobaric process, Vf=2V0V_f = 2V_0 leads to Tf=2T0=2×40 K=80 KT_f = 2T_0 = 2 \times 40 \text{ K} = 80 \text{ K}. The heat input rate for an isobaric process is dQdt=nCPdTdt=(1)(52R)(110)=R4\frac{dQ}{dt} = n C_P \frac{dT}{dt} = (1) (\frac{5}{2}R) (\frac{1}{10}) = \frac{R}{4}, which matches the given rate.