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A metal bar increases in length by 0.05% when heated from 0°C to 100°C. Calculate its coefficient of linear expansion and the percentage increase in its volume.

Physics

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Part 15b(i): Coefficient of linear expansion

  1. Determine the change in temperature and fractional change in length.

    The temperature change is ΔT=100∘C−0∘C=100∘C\Delta T = 100^\circ\text{C} - 0^\circ\text{C} = 100^\circ\text{C}.
    The percentage increase in length is 0.05%0.05\%, so the fractional increase in length is ΔLL0=0.05100=0.0005\frac{\Delta L}{L_0} = \frac{0.05}{100} = 0.0005.

  2. Calculate the coefficient of linear expansion (α\alpha).

    The formula for linear expansion is ΔL=αL0ΔT\Delta L = \alpha L_0 \Delta T. Rearranging for α\alpha:

    α=ΔLL0ΔT=0.0005100∘C\alpha = \frac{\Delta L}{L_0 \Delta T} = \frac{0.0005}{100^\circ\text{C}} α=0.000005 /∘C\alpha = 0.000005 \text{ /}^\circ\text{C} α=5.0×10−6 /∘C\alpha = 5.0 \times 10^{-6} \text{ /}^\circ\text{C}

    The coefficient of linear expansion is:

    5.0×10−6 /∘C\boxed{5.0 \times 10^{-6} \text{ /}^\circ\text{C}}

    Part 15b(ii): Percentage increase of the volume of the bar

  3. Relate the coefficient of volume expansion (γ\gamma) to the coefficient of linear expansion (α\alpha).

    For isotropic materials, the coefficient of volume expansion is approximately three times the coefficient of linear expansion:

    γ=3α\gamma = 3\alpha γ=3×(5.0×10−6 /∘C)=1.5×10−5 /∘C\gamma = 3 \times (5.0 \times 10^{-6} \text{ /}^\circ\text{C}) = 1.5 \times 10^{-5} \text{ /}^\circ\text{C}
  4. Calculate the percentage increase in volume.

    The fractional increase in volume is ΔVV0=γΔT\frac{\Delta V}{V_0} = \gamma \Delta T.

    ΔVV0=(1.5×10−5 /∘C)×(100∘C)\frac{\Delta V}{V_0} = (1.5 \times 10^{-5} \text{ /}^\circ\text{C}) \times (100^\circ\text{C}) ΔVV0=0.0015\frac{\Delta V}{V_0} = 0.0015

    To express this as a percentage:

    Percentage increase=0.0015×100%=0.15%\text{Percentage increase} = 0.0015 \times 100\% = 0.15\%

    The percentage increase of the volume of the bar is:

    0.15%\boxed{0.15\%}

    Part 16a(i): Quantity that remains constant for thermodynamic processes

    • A) Isobaric process: Pressure (PP)
    • B) Isochoric process: Volume (VV)
    • C) Isothermal process: Temperature (TT)
    • D) Adiabatic process: Heat exchange (Q=0Q=0)

    Part 16a(ii): Show that PVγ=constantPV^\gamma = \text{constant} for a monatomic ideal gas undergoing an adiabatic process

  5. State the First Law of Thermodynamics for an adiabatic process.

    For an adiabatic process, there is no heat exchange, so dQ=0dQ = 0.
    The First Law of Thermodynamics states dQ=dU+dWdQ = dU + dW.
    Therefore, dU+dW=0dU + dW = 0.

  6. Express dUdU and dWdW for an ideal gas.

    For an ideal gas, the change in internal energy is dU=nCvdTdU = nC_v dT, where nn is the number of moles and CvC_v is the molar specific heat at constant volume.
    The work done by the gas is dW=PdVdW = P dV.
    Substituting these into the equation from Step 1:

    nCvdT+PdV=0(1)nC_v dT + P dV = 0 \quad (1)
  7. Use the ideal gas law to relate dTdT to dPdP and dVdV.

    The ideal gas law is PV=nRTPV = nRT. Differentiating both sides:

    PdV+VdP=nRdTP dV + V dP = nR dT

    Rearranging for dTdT:

    dT=PdV+VdPnR(2)dT = \frac{P dV + V dP}{nR} \quad (2)
  8. Substitute dTdT into equation (1) and simplify.

    Substitute (2) into (1):

    nCv(PdV+VdPnR)+PdV=0nC_v \left(\frac{P dV + V dP}{nR}\right) + P dV = 0 CvR(PdV+VdP)+PdV=0\frac{C_v}{R} (P dV + V dP) + P dV = 0

    We know that R=Cp−CvR = C_p - C_v, where CpC_p is the molar specific heat at constant pressure. So, CvCp−Cv(PdV+VdP)+PdV=0\frac{C_v}{C_p - C_v} (P dV + V dP) + P dV = 0.
    Divide by CvC_v:

    1CpCv−1(PdV+VdP)+PdVCv=0\frac{1}{\frac{C_p}{C_v} - 1} (P dV + V dP) + \frac{P dV}{C_v} = 0

    Let γ=CpCv\gamma = \frac{C_p}{C_v} (the adiabatic index).

    1γ−1(PdV+VdP)+PdV=0\frac{1}{\gamma - 1} (P dV + V dP) + P dV = 0

    Multiply by (γ−1)(\gamma - 1):

    PdV+VdP+(γ−1)PdV=0P dV + V dP + (\gamma - 1) P dV = 0 VdP+PdV+γPdV−PdV=0V dP + P dV + \gamma P dV - P dV = 0 VdP+γPdV=0V dP + \gamma P dV = 0
  9. Integrate the differential equation.

    Divide the equation by PVPV:

    dPP+γdVV=0\frac{dP}{P} + \gamma \frac{dV}{V} = 0

    Integrate both sides:

    ∫dPP+γ∫dVV=∫0\int \frac{dP}{P} + \gamma \int \frac{dV}{V} = \int 0 ln⁡P+γln⁡V=constant\ln P + \gamma \ln V = \text{constant} ln⁡P+ln⁡Vγ=constant\ln P + \ln V^\gamma = \text{constant} ln⁡(PVγ)=constant\ln (PV^\gamma) = \text{constant}

    Exponentiating both sides:

    PVγ=econstantPV^\gamma = e^{\text{constant}}

    Since econstante^{\text{constant}} is also a constant, we have:

    PVγ=constant\boxed{PV^\gamma = \text{constant}}

    Part 16b(i): Efficiency for a Carnot cycle

    A) As a function of the heat that flows to and from the reservoirs:

    η=1−QCQH\boxed{\eta = 1 - \frac{Q_C}{Q_H}}

    where QCQ_C is the heat rejected to the cold reservoir and QHQ_H is the heat absorbed from the hot reservoir.

    B) As a function of the temperatures of the two reservoirs:

    η=1−TCTH\boxed{\eta = 1 - \frac{T_C}{T_H}}
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