Thermal Physics

170 questions

Question 101Question

A composite cylindrical bar consists of two uniform sections of equal length joined end-to-end. Section A has a radius of 2.0 cm2.0\text{ cm} and a thermal conductivity of 300 W m1K1300\text{ W m}^{-1}\text{K}^{-1}. Section B has a radius of 4.0 cm4.0\text{ cm} and a thermal conductivity of 150 W m1K1150\text{ W m}^{-1}\text{K}^{-1}. The outer end of Section A is maintained at a constant temperature of 120C120^\circ\text{C}, while the outer end of Section B is held at 0C0^\circ\text{C}. Assuming the curved surfaces of both sections are perfectly insulated and heat flow is steady, what is the temperature at the junction between the two sections in C^\circ\text{C}?

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Answer: 40

Answer

The steady-state temperature at the junction between Section A and Section B is 40.0°C.
At steady state, the rate of heat conduction through Section A equals that through Section B. Because Section B has double the radius of Section A, its cross-sectional area is four times as large. Equating the heat flow rates gives 300 * A_A * (120 - T_J) = 150 * (4 A_A) * T_J, which simplifies directly to 120 - T_J = 2 T_J, yielding a junction temperature of 40.0°C.

Step-by-Step Solution

1
Determine the relationship between the cross-sectional areas of Section A and Section B.
The area ratio A_B / A_A = (r_B / r_A)² = (4.0 cm / 2.0 cm)² = 4.
The cross-sectional area of a cylinder is proportional to the square of its radius.
2
Write the steady-state heat flow equation for each section.
H_A = (k_A * A_A * (120 - T_J)) / L and H_B = (k_B * A_B * (T_J - 0)) / L.
According to Fourier's law of thermal conduction, the heat transfer rate through a uniform layer is proportional to thermal conductivity, cross-sectional area, and temperature difference, and inversely proportional to length.
3
Equate the heat transfer rates H_A and H_B and solve for the junction temperature T_J.
300 * A_A * (120 - T_J) = 150 * (4 A_A) * T_J => 300 * (120 - T_J) = 600 * T_J => 120 - T_J = 2 T_J => 3 T_J = 120 => T_J = 40.0°C.
At steady state with insulated sides, heat does not accumulate or escape, so the rate of heat conduction through both sections must be identical.

Key Concept

Steady-state thermal conduction through composite conductors with differing cross-sectional areas and thermal conductivities
Question 102Question

A cylindrical copper rod of thermal conductivity 380 Wm1K1380\text{ W}\cdot\text{m}^{-1}\cdot\text{K}^{-1}, length 0.40 m0.40\text{ m}, and uniform radius 2.0 cm2.0\text{ cm} is thermally insulated along its curved surface. One flat end is maintained at a temperature of 100C100^\circ\text{C} by steam, while the opposite end is kept in an ice bath at 0C0^\circ\text{C}. Assuming steady-state heat conduction, what is the rate of heat flow through the rod? (Take π=3.14\pi = 3.14)

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Answer: 119.3 W119.3\text{ W}

Answer

The rate of heat flow through the copper rod is 119.3 W119.3\text{ W}.
According to Fourier's law of heat conduction, the rate of thermal energy transfer Qt\frac{Q}{t} through a material of thermal conductivity kk, cross-sectional area AA, and length dd across temperature difference ΔT\Delta T is given by Qt=kAΔTd\frac{Q}{t} = \frac{k A \Delta T}{d}. Substituting k=380 Wm1K1k = 380\text{ W}\cdot\text{m}^{-1}\cdot\text{K}^{-1}, A=π(0.02 m)2=1.256×103 m2A = \pi (0.02\text{ m})^2 = 1.256 \times 10^{-3}\text{ m}^2, ΔT=100 K\Delta T = 100\text{ K}, and d=0.40 md = 0.40\text{ m} yields 119.3 W119.3\text{ W}.

Step-by-Step Solution

1
Convert the radius from centimeters to meters and calculate the cross-sectional area of the rod.
r=2.0 cm=0.02 mr = 2.0\text{ cm} = 0.02\text{ m}. A=πr2=3.14×(0.02 m)2=1.256×103 m2A = \pi r^2 = 3.14 \times (0.02\text{ m})^2 = 1.256 \times 10^{-3}\text{ m}^2.
Fourier's law requires the area in square meters (m2m^2).
2
Determine the temperature difference across the rod.
ΔT=100C0C=100 K\Delta T = 100^\circ\text{C} - 0^\circ\text{C} = 100\text{ K}.
Heat transfer rate depends on the temperature gradient along the length.
3
Apply Fourier's law of thermal conduction: Qt=kAΔTd\frac{Q}{t} = \frac{k A \Delta T}{d}.
Qt=380×1.256×103×1000.40=119.32 W119.3 W\frac{Q}{t} = \frac{380 \times 1.256 \times 10^{-3} \times 100}{0.40} = 119.32\text{ W} \approx 119.3\text{ W}.
Substituting the thermal conductivity kk, cross-sectional area AA, temperature difference ΔT\Delta T, and length dd gives the steady-state heat conduction rate.

Key Concept

Fourier's Law of Heat Conduction in solids: Qt=kA(ThotTcold)d\frac{Q}{t} = \frac{k A (T_{\text{hot}} - T_{\text{cold}})}{d}
Estimated Time:2m 0s
Question 103Question

Two rectangular slabs of equal thickness dd are mounted in parallel between a hot reservoir at 100C100^\circ\text{C} and a cold reservoir at 20C20^\circ\text{C}. Slab 1 has a thermal conductivity k1=300 Wm1K1k_1 = 300\text{ W}\cdot\text{m}^{-1}\cdot\text{K}^{-1} and a cross-sectional area A1=4.0×104 m2A_1 = 4.0 \times 10^{-4}\text{ m}^2. Slab 2 has a thermal conductivity k2=100 Wm1K1k_2 = 100\text{ W}\cdot\text{m}^{-1}\cdot\text{K}^{-1} and a cross-sectional area A2=6.0×104 m2A_2 = 6.0 \times 10^{-4}\text{ m}^2. Assuming steady-state heat conduction and no lateral heat loss, what percentage of the total heat transferred per second between the reservoirs conducts through Slab 1?

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Answer: 66.7%66.7\%

Answer

The percentage of the total heat transferred per second conducted through Slab 1 is 66.7%.
Fourier's law gives the rate of heat conduction as P=kAΔTdP = \frac{k A \Delta T}{d}. Since the temperature gradient ΔTd\frac{\Delta T}{d} is identical across both parallel slabs, the heat current through each slab is directly proportional to its kAk A product. For Slab 1, k1A1=300×4.0×104=0.12k_1 A_1 = 300 \times 4.0 \times 10^{-4} = 0.12, while for Slab 2, k2A2=100×6.0×104=0.06k_2 A_2 = 100 \times 6.0 \times 10^{-4} = 0.06. The total heat current is proportional to 0.12+0.06=0.180.12 + 0.06 = 0.18. Thus, the fraction conducted through Slab 1 is 0.120.18=23\frac{0.12}{0.18} = \frac{2}{3}, which corresponds to 66.7%66.7\%.

Step-by-Step Solution

1
Express Fourier's law of heat conduction for each slab in parallel.
Rate of heat flow P1=k1A1ΔTdP_1 = \frac{k_1 A_1 \Delta T}{d} and P2=k2A2ΔTdP_2 = \frac{k_2 A_2 \Delta T}{d}.
Both slabs experience the same temperature difference ΔT=100C20C=80 K\Delta T = 100^\circ\text{C} - 20^\circ\text{C} = 80\text{ K} and have equal length dd.
2
Calculate the effective conductance factors kAk A for both slabs.
k1A1=300×(4.0×104)=0.12 WmK1k_1 A_1 = 300 \times (4.0 \times 10^{-4}) = 0.12\text{ W}\cdot\text{m}\cdot\text{K}^{-1} and k2A2=100×(6.0×104)=0.06 WmK1k_2 A_2 = 100 \times (6.0 \times 10^{-4}) = 0.06\text{ W}\cdot\text{m}\cdot\text{K}^{-1}.
Since ΔT/d\Delta T / d is identical for both parallel paths, the heat flow rate is directly proportional to kAk A.
3
Determine the total heat flow rate and the percentage carried by Slab 1.
Ptotal=P1+P20.12+0.06=0.18P_{\text{total}} = P_1 + P_2 \propto 0.12 + 0.06 = 0.18. Percentage through Slab 1 =0.120.18×100%=66.7%= \frac{0.12}{0.18} \times 100\% = 66.7\%.
In parallel conduction, individual heat currents add to form the total heat current.

Key Concept

Parallel Thermal Conduction
Question 104Question

Two solid cylindrical copper rods, PP and QQ, are maintained under identical temperature differences across their ends. Rod PP has twice the radius and half the length of Rod QQ. What is the ratio of the rate of heat conduction through Rod PP to that through Rod QQ?

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Answer: 8:18 : 1

Answer

The ratio of the rate of heat conduction through Rod PP to that through Rod QQ is 8:18 : 1.
The rate of heat conduction is given by Qt=kπr2ΔTL\frac{Q}{t} = \frac{k \pi r^2 \Delta T}{L}. For Rod PP, substituting rP=2rQr_P = 2 r_Q and LP=0.5LQL_P = 0.5 L_Q gives (2)20.5=8\frac{(2)^2}{0.5} = 8 times the rate of Rod QQ. Thus, the ratio of heat conduction rate is 8:18 : 1.

Step-by-Step Solution

1
Write the fundamental equation for the rate of thermal conduction through a uniform conductor.
Qt=kAΔTL\frac{Q}{t} = \frac{k A \Delta T}{L}
Heat conduction rate is proportional to thermal conductivity kk, cross-sectional area AA, temperature difference ΔT\Delta T, and inversely proportional to length LL.
2
Express the cross-sectional area AA in terms of radius rr for a cylindrical rod.
A=πr2    Qt=kπr2ΔTLA = \pi r^2 \implies \frac{Q}{t} = \frac{k \pi r^2 \Delta T}{L}
The cross-section of a cylindrical rod is a circle.
3
Set up the ratio of heat conduction rates for Rod PP and Rod QQ given rP=2rQr_P = 2 r_Q and LP=0.5LQL_P = 0.5 L_Q.
(Q/t)P(Q/t)Q=rP2/LPrQ2/LQ=(2rQ)2/(0.5LQ)rQ2/LQ=40.5=8\frac{(Q/t)_P}{(Q/t)_Q} = \frac{r_P^2 / L_P}{r_Q^2 / L_Q} = \frac{(2 r_Q)^2 / (0.5 L_Q)}{r_Q^2 / L_Q} = \frac{4}{0.5} = 8
Material (kk) and temperature difference (ΔT\Delta T) are identical for both rods and cancel out.

Key Concept

Thermal Conduction Rate Formula
Question 105Question

Match each heat transfer process or physical phenomenon on the left with its underlying governing mechanism or quantitative relationship on the right.

Click a left item, then click its matching right item

Items

Steady-state rate of heat conduction through a uniform plane slab of cross-sectional area AA
Total radiant energy emitted per unit time per unit surface area by an ideal blackbody radiator
Natural heat transport mechanism in fluids under the influence of a gravitational field
Dominant microscopic thermal conduction mechanism in solid electrical insulators

Matches

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Answer

The steady-state rate of heat conduction through a uniform slab corresponds to being directly proportional to the temperature gradient. The radiant energy emitted per unit area by an ideal blackbody corresponds to being directly proportional to the fourth power of absolute temperature. Natural heat transport in fluids under gravity corresponds to being driven by buoyant forces resulting from density variations. The microscopic conduction mechanism in electrical insulators corresponds to propagation via quantized lattice vibrations (phonons).
Each heat transfer mechanism matches its fundamental law and microscopic process: conduction across a plane wall is governed by Fourier's law and proportional to the temperature gradient; thermal radiation from a blackbody obeys Stefan's law and scales with the fourth power of absolute temperature; natural convection in fluids requires gravity to drive density-based buoyant circulation; and thermal conduction in non-metallic insulators relies on atomic lattice vibrations (phonons) due to the absence of free electrons.

Step-by-Step Solution

1
Analyze conduction governing equation (Fourier's Law)
Heat current Qt=kAΔTd\frac{Q}{t} = kA \frac{\Delta T}{d}, showing that heat flow per unit area depends directly on the temperature gradient ΔTΔx\frac{\Delta T}{\Delta x}.
Identify the quantitative relationship governing thermal conduction in solid materials.
2
Analyze radiation power equation (Stefan-Boltzmann Law)
Total power per unit area P/A=σT4P/A = \sigma T^4, establishing fourth-power dependence on thermodynamic temperature TT.
Identify the law governing thermal radiation emissions.
3
Examine natural convection mechanics
Thermal expansion leads to density differences Δρ\Delta \rho, causing buoyant forces under gravity to set up fluid circulation currents.
Identify the physical drive behind natural convection in fluids.
4
Examine microscopic heat transfer mechanisms in insulators
Insulators lack mobile valence electrons, leaving atomic lattice vibrations (phonons) as the sole mechanism for thermal energy transport.
Distinguish between electronic conduction in metals and lattice/phonon conduction in non-metals.

Key Concept

Physical Principles and Microscopic Mechanisms of Conduction, Convection, and Radiation
Question 106Question

The specific heat capacity of a physical body increases proportionally with its mass, whereas its total heat capacity remains constant for any quantity of a given material.

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Answer: False

Answer

The statement is False. Specific heat capacity is an intensive property independent of mass, whereas heat capacity is an extensive property that depends directly on mass.
The statement is false because specific heat capacity (cc) is an intensive property that remains constant regardless of mass, while heat capacity (CC) is an extensive property that increases directly with the mass of the object.

Step-by-Step Solution

1
Recall the mathematical definitions of heat capacity and specific heat capacity
Heat capacity C=QΔT=mcC = \frac{Q}{\Delta T} = mc, whereas specific heat capacity c=QmΔTc = \frac{Q}{m\Delta T}.
Establishing the functional dependence of both thermal quantities on mass.
2
Compare intensive and extensive classifications
Specific heat capacity cc is normalized per unit mass (J kg1 K1\text{J kg}^{-1}\text{ K}^{-1}) and is independent of mass. Heat capacity CC (J K1\text{J K}^{-1}) scales directly with mass mm.
The statement falsely reverses which quantity depends on mass.

Key Concept

Distinguishing between extensive (heat capacity) and intensive (specific heat capacity) thermal properties
Estimated Time:1m 0s
Question 107Question

A sample of gas enclosed in a vessel has a density of 0.90 kg/m30.90\text{ kg/m}^3 and exerts a pressure of 3.0×105 N/m23.0 \times 10^5\text{ N/m}^2 on the walls of the vessel. Based on the kinetic theory of gases, what is the root-mean-square (r.m.s.) speed of the gas molecules in m/s\text{m/s}?

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Answer: 1000

Answer

The root-mean-square speed of the gas molecules is 1000 m/s1000\text{ m/s}.
By applying the kinetic theory formula P=13ρvrms2P = \frac{1}{3} \rho v_{\text{rms}}^2, rearranging gives vrms=3Pρv_{\text{rms}} = \sqrt{\frac{3P}{\rho}}. Substituting P=3.0×105 N/m2P = 3.0 \times 10^5\text{ N/m}^2 and ρ=0.90 kg/m3\rho = 0.90\text{ kg/m}^3 results in vrms=9.0×1050.90=1.0×106=1000 m/sv_{\text{rms}} = \sqrt{\frac{9.0 \times 10^5}{0.90}} = \sqrt{1.0 \times 10^6} = 1000\text{ m/s}.

Step-by-Step Solution

1
Identify the kinetic theory equation relating gas pressure, density, and microscopic molecular speed.
P=13ρvrms2P = \frac{1}{3} \rho v_{\text{rms}}^2
According to the kinetic theory of gases, the macroscopic pressure exerted by gas molecules colliding with container walls is proportional to the gas density and the square of their r.m.s. speed.
2
Make vrmsv_{\text{rms}} the subject of the formula.
vrms=3Pρv_{\text{rms}} = \sqrt{\frac{3P}{\rho}}
Multiplying both sides by 33 and dividing by density ρ\rho isolates vrms2v_{\text{rms}}^2, taking the square root yields vrmsv_{\text{rms}}.
3
Substitute the given numerical values into the equation.
vrms=3×3.0×1050.90=1,000,000=1000 m/sv_{\text{rms}} = \sqrt{\frac{3 \times 3.0 \times 10^5}{0.90}} = \sqrt{1,000,000} = 1000\text{ m/s}
Performing the division yields 1.0×106 m2/s21.0 \times 10^6\text{ m}^2/\text{s}^2, whose square root gives the speed in m/s\text{m/s}.

Key Concept

Kinetic Theory Pressure Equation relating macroscopic pressure and density to microscopic root-mean-square velocity (P=13ρvrms2P = \frac{1}{3}\rho v_{\text{rms}}^2).
Question 108Question

Match each thermometer type on the left with its corresponding physical thermometric property on the right.

Click a left item, then click its matching right item

Items

Constant-volume gas thermometer
Thermocouple
Platinum resistance thermometer
Liquid-in-glass thermometer

Matches

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Answer

Constant-volume gas thermometer matches variation of gas pressure at constant volume; Thermocouple matches variation of electromotive force (e.m.f.); Platinum resistance thermometer matches variation of electrical resistance; Liquid-in-glass thermometer matches variation of liquid column length/volume.
Each thermometer is paired with its corresponding thermometric property: constant-volume gas thermometer relies on gas pressure variation, thermocouple relies on thermoelectric e.m.f. variation, resistance thermometer relies on electrical resistance variation, and liquid-in-glass thermometer relies on liquid thermal expansion.

Step-by-Step Solution

1
Identify the thermometric property for a constant-volume gas thermometer.
Gas pressure at constant volume.
Pressure varies linearly with temperature for an ideal gas at constant volume.
2
Identify the thermometric property for a thermocouple.
Electromotive force (e.m.f.).
The thermoelectric effect generates an e.m.f. proportional to the temperature difference between two junctions.
3
Identify the thermometric property for a platinum resistance thermometer.
Electrical resistance.
The electrical resistance of platinum increases continuously and predictably with temperature.
4
Identify the thermometric property for a liquid-in-glass thermometer.
Liquid column length/volume.
The liquid expands linearly along the capillary stem as temperature rises.

Key Concept

Thermometric Properties of Thermometers
Question 109Question

A thermocouple thermometer produces an electromotive force (e.m.f.) of 2.0mV2.0\,\text{mV} at the ice point (0C0^\circ\text{C}) and 18.0mV18.0\,\text{mV} at the steam point (100C100^\circ\text{C}). When placed in a liquid bath, the recorded e.m.f. is 14.0mV14.0\,\text{mV}. What is the temperature of the liquid bath on the Celsius scale?

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Answer: 75.0C75.0^\circ\text{C}

Answer

75.0C75.0^\circ\text{C}
The temperature on a linear scale is proportional to the fraction of the interval traversed between the fixed points. Subtracting the baseline reading of 2.0mV2.0\,\text{mV} gives an effective increase of 12.0mV12.0\,\text{mV} out of a total range of 16.0mV16.0\,\text{mV}. Multiplying this fraction (0.750.75) by 100C100^\circ\text{C} yields 75.0C75.0^\circ\text{C}.

Step-by-Step Solution

1
Identify the given thermometric values for the lower fixed point, upper fixed point, and unknown temperature reading.
E0=2.0mVE_0 = 2.0\,\text{mV}, E100=18.0mVE_{100} = 18.0\,\text{mV}, and Eθ=14.0mVE_\theta = 14.0\,\text{mV}.
Linear temperature scales relate the change in thermometric property proportionally to temperature changes.
2
Apply the standard linear interpolation formula for a Celsius temperature scale.
θ=EθE0E100E0×100C\theta = \frac{E_\theta - E_0}{E_{100} - E_0} \times 100^\circ\text{C}
This accounts for the baseline reading at the ice point (0C0^\circ\text{C}) and normalizes it over the 100C100^\circ\text{C} fundamental interval.
3
Substitute the known values and evaluate the expression.
θ=14.02.018.02.0×100=12.016.0×100=0.75×100=75.0C\theta = \frac{14.0 - 2.0}{18.0 - 2.0} \times 100 = \frac{12.0}{16.0} \times 100 = 0.75 \times 100 = 75.0^\circ\text{C}.
Carrying out the subtraction yields a proportional change of 34\frac{3}{4} of the full fundamental interval.

Key Concept

Temperature Scale Calibration and Thermocouple Interpolation
Estimated Time:1m 30s
Question 110Question

A constant-volume gas thermometer registers a pressure of 60kPa60\,\text{kPa} at the ice point (0C0^\circ\text{C}) and 84kPa84\,\text{kPa} at the steam point (100C100^\circ\text{C}). What is the temperature in degrees Celsius when the pressure registered by the thermometer is 72kPa72\,\text{kPa}?

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Answer: 50

Answer

The temperature corresponding to a pressure reading of 72kPa72\,\text{kPa} is 50C50^\circ\text{C}.
Using the linear relation for a constant-volume gas thermometer: T=PTP0P100P0×100CT = \frac{P_T - P_0}{P_{100} - P_0} \times 100^\circ\text{C}. Substituting PT=72kPaP_T = 72\,\text{kPa}, P0=60kPaP_0 = 60\,\text{kPa}, and P100=84kPaP_{100} = 84\,\text{kPa} yields T=72608460×100=1224×100=50CT = \frac{72 - 60}{84 - 60} \times 100 = \frac{12}{24} \times 100 = 50^\circ\text{C}.

Step-by-Step Solution

1
Identify the thermometric property values at the fixed points and target state.
P0=60kPaP_0 = 60\,\text{kPa}, P100=84kPaP_{100} = 84\,\text{kPa}, and PT=72kPaP_T = 72\,\text{kPa}.
These represent the pressure values corresponding to 0C0^\circ\text{C}, 100C100^\circ\text{C}, and the unknown temperature TT respectively.
2
Set up the linear scale conversion equation.
T=PTP0P100P0×100CT = \frac{P_T - P_0}{P_{100} - P_0} \times 100^\circ\text{C}
Temperature changes linearly with the thermometric property (gas pressure at constant volume).
3
Calculate the numerical value.
T=1224×100=50CT = \frac{12}{24} \times 100 = 50^\circ\text{C}
Simplifying the fraction 1224=0.5\frac{12}{24} = 0.5 and multiplying by 100100 gives 5050.

Key Concept

Temperature measurement using constant-volume gas pressure as a thermometric property
Question 111Question

If a sample of unsaturated air with a relative humidity of 40%40\% at 30C30^\circ\text{C} is compressed isothermally to one-third of its original volume, the final relative humidity of the air will be 100%100\%.

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Answer: True

Answer

True. The relative humidity cannot exceed 100% because water vapour condenses into liquid once its partial pressure reaches the saturated vapour pressure at that temperature.
The statement is true because relative humidity is the ratio of actual partial vapour pressure to saturated vapour pressure at a specific temperature. Although isothermal compression to one-third volume triples the partial pressure of water vapour (giving a theoretical 120%), partial vapour pressure is bounded by the saturated vapour pressure. When the relative humidity reaches 100%, condensation occurs, keeping the relative humidity at exactly 100%.

Step-by-Step Solution

1
Apply Boyle's law to calculate the theoretical partial vapour pressure after isothermal compression.
Since volume is reduced to 13V1\frac{1}{3}V_1 at constant temperature, the partial pressure of water vapour would increase by a factor of 3 (p2=3p1p_2 = 3p_1).
For an unsaturated vapour at constant temperature, partial pressure is inversely proportional to volume.
2
Determine the theoretical relative humidity from the pressure ratio.
\text{Theoretical R.H.} = 3 \times 40\% = 120\%.
Relative humidity is defined as R.H.=pps×100%\text{R.H.} = \frac{p}{p_s} \times 100\%, where pp is the partial pressure and psp_s is the saturated vapour pressure.
3
Apply the physical limit imposed by saturated vapour pressure.
The actual relative humidity cannot exceed 100%100\%; excess vapour condenses.
Saturated vapour pressure psp_s represents the maximum possible partial pressure of water vapour in air at a given temperature.

Key Concept

Saturated Vapour Pressure Limit and Relative Humidity under Isothermal Compression
Question 112Question

A composite solid consists of a metal block AA of mass 2.0 kg2.0\text{ kg} and a metal block BB of mass 1.0 kg1.0\text{ kg} joined in thermal contact. Block AA has a specific heat capacity of 300 J kg1K1300\text{ J kg}^{-1}\text{K}^{-1}. When the composite solid absorbs 18 kJ18\text{ kJ} of thermal energy, its overall temperature increases by 15 K15\text{ K}. Assuming no heat loss to the surroundings, what is the specific heat capacity of metal block BB?

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Answer: 600 J kg1K1600\text{ J kg}^{-1}\text{K}^{-1}

Answer

600 J kg1K1600\text{ J kg}^{-1}\text{K}^{-1}
The total heat energy supplied (18 kJ=18000 J18\text{ kJ} = 18000\text{ J}) causes a temperature rise of 15 K15\text{ K}, giving a total heat capacity Ctotal=1200 J K1C_{\text{total}} = 1200\text{ J K}^{-1} for the composite solid. Subtracting block AA's heat capacity (CA=2.0 kg×300 J kg1K1=600 J K1C_A = 2.0\text{ kg} \times 300\text{ J kg}^{-1}\text{K}^{-1} = 600\text{ J K}^{-1}) leaves a heat capacity of 600 J K1600\text{ J K}^{-1} for block BB. Dividing block BB's heat capacity by its mass (1.0 kg1.0\text{ kg}) yields its specific heat capacity of 600 J kg1K1600\text{ J kg}^{-1}\text{K}^{-1}.

Step-by-Step Solution

1
Calculate the total heat capacity (CtotalC_{\text{total}}) of the composite system.
Ctotal=QΔT=18000 J15 K=1200 J K1C_{\text{total}} = \frac{Q}{\Delta T} = \frac{18000\text{ J}}{15\text{ K}} = 1200\text{ J K}^{-1}
Heat capacity is defined as the total heat energy absorbed per unit change in temperature.
2
Determine the heat capacity (CAC_A) of metal block AA.
CA=mA×cA=2.0 kg×300 J kg1K1=600 J K1C_A = m_A \times c_A = 2.0\text{ kg} \times 300\text{ J kg}^{-1}\text{K}^{-1} = 600\text{ J K}^{-1}
Heat capacity is the product of mass and specific heat capacity.
3
Determine the heat capacity (CBC_B) of metal block BB.
CB=CtotalCA=1200 J K1600 J K1=600 J K1C_B = C_{\text{total}} - C_A = 1200\text{ J K}^{-1} - 600\text{ J K}^{-1} = 600\text{ J K}^{-1}
Total heat capacity of a composite body is the sum of the individual heat capacities of its components.
4
Calculate the specific heat capacity (cBc_B) of metal block BB.
cB=CBmB=600 J K11.0 kg=600 J kg1K1c_B = \frac{C_B}{m_B} = \frac{600\text{ J K}^{-1}}{1.0\text{ kg}} = 600\text{ J kg}^{-1}\text{K}^{-1}
Specific heat capacity is the heat capacity per unit mass of that specific substance.

Key Concept

Additivity of Heat Capacity in Composite Systems (Ctotal=mAcA+mBcBC_{\text{total}} = m_A c_A + m_B c_B)
Question 113Question

A mass of air at 30C30^\circ\text{C} has a relative humidity of 50%50\%. The saturated vapour pressure of water is 30 mmHg30\text{ mmHg} at 30C30^\circ\text{C} and 9 mmHg9\text{ mmHg} at 10C10^\circ\text{C}. If the temperature of the air is lowered to 10C10^\circ\text{C}, what percentage of the initial water vapour condenses out?

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Answer: $40\%

Answer

The percentage of initial water vapour that condenses out when cooled to 10C10^\circ\text{C} is 40%40\%.
The correct answer is 40%40\%. Initially, the air contains water vapour exerting a partial pressure of 0.50×30 mmHg=15 mmHg0.50 \times 30\text{ mmHg} = 15\text{ mmHg}. Upon cooling to 10C10^\circ\text{C}, the air becomes saturated at 9 mmHg9\text{ mmHg}, causing 15 mmHg9 mmHg=6 mmHg15\text{ mmHg} - 9\text{ mmHg} = 6\text{ mmHg} worth of vapour to condense into liquid. The condensed amount as a fraction of the initial vapour is 6/15=0.406 / 15 = 0.40, or 40%40\%.

Step-by-Step Solution

1
Calculate the initial partial vapour pressure of water at 30C30^\circ\text{C}.
Partial Vapour Pressure=Relative Humidity×SVP at 30C=0.50×30 mmHg=15 mmHg\text{Partial Vapour Pressure} = \text{Relative Humidity} \times \text{SVP at } 30^\circ\text{C} = 0.50 \times 30\text{ mmHg} = 15\text{ mmHg}.
Relative humidity is the ratio of actual partial vapour pressure to the saturated vapour pressure at that temperature.
2
Determine the amount of vapour pressure that must condense when cooled to 10C10^\circ\text{C}.
Vapour pressure condensed=15 mmHg9 mmHg=6 mmHg\text{Vapour pressure condensed} = 15\text{ mmHg} - 9\text{ mmHg} = 6\text{ mmHg}.
At 10C10^\circ\text{C}, the air can hold at most its saturated vapour pressure of 9 mmHg9\text{ mmHg}, so any excess vapour above 9 mmHg9\text{ mmHg} condenses into liquid water.
3
Calculate the percentage of the initial water vapour that condenses out.
Percentage condensed=(6 mmHg15 mmHg)×100%=40%\text{Percentage condensed} = \left(\frac{6\text{ mmHg}}{15\text{ mmHg}}\right) \times 100\% = 40\%.
The question asks for the fraction of the initial vapour originally present that leaves the gaseous state.

Key Concept

Relative Humidity and Dew Point Condensation
Estimated Time:1m 30s
Question 114Question

A solid cylindrical metal rod of length 0.50 m0.50\text{ m} and cross-sectional area 4.0×104 m24.0 \times 10^{-4}\text{ m}^2 is perfectly insulated along its lateral surface. One end of the rod is maintained at 100C100^\circ\text{C} in boiling water, while the other end is in contact with an ice block at 0C0^\circ\text{C}. If 0.072 kg0.072\text{ kg} of ice melts in 10 minutes10\text{ minutes} due to thermal energy conducted through the rod, what is the thermal conductivity of the metal? (Take the specific latent heat of fusion of ice as 3.36×105 Jkg13.36 \times 10^5\text{ J}\cdot\text{kg}^{-1})

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Answer: 504 Wm1K1504\text{ W}\cdot\text{m}^{-1}\cdot\text{K}^{-1}

Answer

The thermal conductivity of the metal rod is 504 Wm1K1504\text{ W}\cdot\text{m}^{-1}\cdot\text{K}^{-1}.
The correct answer is derived by first finding the total heat absorbed during the phase change of ice using Q=mL=0.072×3.36×105=24,192 JQ = m L = 0.072 \times 3.36 \times 10^5 = 24,192\text{ J}. Dividing by the time in seconds (600 s600\text{ s}) gives a heat flow rate of 40.32 W40.32\text{ W}. Substituting this into the conduction formula Qt=kAΔTd\frac{Q}{t} = \frac{k A \Delta T}{d} gives 40.32=k(4.0×104)(100)0.50=0.08k40.32 = \frac{k (4.0 \times 10^{-4})(100)}{0.50} = 0.08 k, yielding k=504 Wm1K1k = 504\text{ W}\cdot\text{m}^{-1}\cdot\text{K}^{-1}.

Step-by-Step Solution

1
Calculate the total heat energy QQ required to melt 0.072 kg0.072\text{ kg} of ice at 0C0^\circ\text{C}.
Q=mL=0.072 kg×3.36×105 Jkg1=24,192 JQ = m L = 0.072\text{ kg} \times 3.36 \times 10^5\text{ J}\cdot\text{kg}^{-1} = 24,192\text{ J}
During melting at constant temperature, heat transfer is governed by the latent heat of fusion formula.
2
Convert the elapsed time into seconds and calculate the rate of heat transfer Qt\frac{Q}{t}.
t=10 min=600 st = 10\text{ min} = 600\text{ s}; Qt=24,192 J600 s=40.32 W\frac{Q}{t} = \frac{24,192\text{ J}}{600\text{ s}} = 40.32\text{ W}
Thermal conductivity formulas require rate of heat transfer in Joules per second (Watts).
3
Apply Fourier's law of thermal conduction Qt=kA(T1T2)d\frac{Q}{t} = \frac{k A (T_1 - T_2)}{d} to solve for thermal conductivity kk.
40.32=k×(4.0×104)×(1000)0.50    40.32=0.08k    k=504 Wm1K140.32 = \frac{k \times (4.0 \times 10^{-4}) \times (100 - 0)}{0.50} \implies 40.32 = 0.08 k \implies k = 504\text{ W}\cdot\text{m}^{-1}\cdot\text{K}^{-1}
Rearranging the steady-state thermal conduction equation yields k=(Q/t)dAΔTk = \frac{(Q/t) \cdot d}{A \cdot \Delta T}.

Key Concept

Thermal Conduction Rate and Latent Heat of Fusion
Question 115Question

Match each kinetic theory concept or microscopic property of an ideal gas on the left with its corresponding mathematical expression or derivation result on the right.

Click a left item, then click its matching right item

Items

Magnitude of momentum change (Δpx)(\Delta p_x) for a gas molecule of mass mm colliding elastically with a container wall perpendicular to the x-axis at speed vxv_x
Average force (Fx)(F_x) exerted by a single gas molecule moving back and forth between two parallel walls separated by length LL
Translational kinetic energy per unit volume (EkV)\left(\frac{E_k}{V}\right) of an ideal gas operating at pressure PP
Root-mean-square speed (vrms)(v_{\text{rms}}) of an ideal gas molecule in terms of molar mass MM, universal gas constant RR, and absolute temperature TT

Matches

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Answer

The correct matches pair the momentum change per collision with 2mvx2 m v_x, the single-molecule average wall force with mvx2L\frac{m v_x^2}{L}, the kinetic energy density with 32P\frac{3}{2} P, and the root-mean-square speed with 3RTM\sqrt{\frac{3 R T}{M}}.
Each kinetic theory quantity is derived directly from fundamental principles of mechanics applied to gas particles. Elastic collision with a wall yields a momentum reversal of magnitude 2mvx2 m v_x. Taking the round-trip collision frequency over length LL yields an average force of mvx2L\frac{m v_x^2}{L}. Linking microscopic kinetic energy density to pressure gives EkV=32P\frac{E_k}{V} = \frac{3}{2} P, and linking pressure to the ideal gas law for one mole yields vrms=3RTMv_{\text{rms}} = \sqrt{\frac{3 R T}{M}}.

Step-by-Step Solution

1
Analyze momentum transfer during elastic collision of a molecule with a wall.
Initial momentum along the x-axis is pi=mvxp_i = m v_x and final momentum after elastic reflection is pf=mvxp_f = -m v_x. The change in momentum is Δpx=pfpi=2mvx\Delta p_x = p_f - p_i = -2 m v_x, which has a magnitude of 2mvx2 m v_x.
Elastic collision conserves kinetic energy and reverses velocity direction perpendicular to the wall.
2
Calculate the time rate of momentum transfer to determine average force.
The round-trip distance between opposite walls separated by length LL is 2L2L, so the time between collisions with the same wall is Δt=2Lvx\Delta t = \frac{2L}{v_x}. The average force is Fx=ΔpΔt=2mvx2L/vx=mvx2LF_x = \frac{\Delta p}{\Delta t} = \frac{2 m v_x}{2L / v_x} = \frac{m v_x^2}{L}.
Newton's second law expresses force as the average rate of change of momentum.
3
Relate total translational kinetic energy density to gas pressure.
From kinetic theory, gas pressure is given by P=13NmVvrms2P = \frac{1}{3} \frac{N m}{V} v_{\text{rms}}^2. Since total kinetic energy Ek=12Nmvrms2E_k = \frac{1}{2} N m v_{\text{rms}}^2, we can express pressure as P=23(EkV)P = \frac{2}{3} \left(\frac{E_k}{V}\right). Rearranging gives energy density EkV=32P\frac{E_k}{V} = \frac{3}{2} P.
Translational kinetic energy density is directly proportional to pressure with a factor of 3/2.
4
Derive the formula for root-mean-square velocity from macroscopic and microscopic gas equations.
Substitute density ρ=MV\rho = \frac{M}{V} (where MM is molar mass) into P=13ρvrms2P = \frac{1}{3} \rho v_{\text{rms}}^2, obtaining P=Mvrms23VP = \frac{M v_{\text{rms}}^2}{3 V}. Since PV=RTP V = R T for one mole of ideal gas, RT=13Mvrms2    vrms=3RTMR T = \frac{1}{3} M v_{\text{rms}}^2 \implies v_{\text{rms}} = \sqrt{\frac{3 R T}{M}}.
Connects microscopic speed distribution parameter with thermodynamic temperature and molar mass.

Key Concept

Kinetic Theory of Matter and Pressure of Gases
Question 116Question

In an experiment to determine the specific latent heat of vaporization of water at 100C100^\circ\text{C} using an electric immersion heater in an uninsulated vessel, if heat loss from the vessel to the cooler surrounding environment is neglected in the calculations, the experimentally determined value of the specific latent heat of vaporization will be higher than the true value.

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Answer: True

Answer

True
The statement is correct because the measured energy supplied by the heater includes both the energy required for the phase change and the thermal energy dissipated to the surroundings. Dividing this larger total energy by the mass of vaporized liquid results in an overestimation of the specific latent heat of vaporization.

Step-by-Step Solution

1
Formulate the thermal energy balance equation including heat loss.
Qelectrical=Qvaporization+QlossQ_{\text{electrical}} = Q_{\text{vaporization}} + Q_{\text{loss}}, where Qelectrical=PtQ_{\text{electrical}} = P \cdot t and Qvaporization=mLtrueQ_{\text{vaporization}} = m \cdot L_{\text{true}}.
Energy conservation dictates that the electrical energy supplied by the heater equals the thermal energy used for vaporization plus the heat lost to the cooler ambient surroundings.
2
Express the calculated specific latent heat LcalcL_{\text{calc}} under the assumption of zero heat loss.
Lcalc=Qelectricalm=mLtrue+QlossmL_{\text{calc}} = \frac{Q_{\text{electrical}}}{m} = \frac{m \cdot L_{\text{true}} + Q_{\text{loss}}}{m}.
The experimenter measures the total electrical power and time, assuming all of this energy converted liquid into vapor.
3
Compare the calculated specific latent heat LcalcL_{\text{calc}} with the true value LtrueL_{\text{true}}.
Lcalc=Ltrue+Qlossm>LtrueL_{\text{calc}} = L_{\text{true}} + \frac{Q_{\text{loss}}}{m} > L_{\text{true}}.
Because Qloss>0Q_{\text{loss}} > 0 and mass m>0m > 0, the ratio Qlossm\frac{Q_{\text{loss}}}{m} is positive, meaning LcalcL_{\text{calc}} is higher than LtrueL_{\text{true}}.

Key Concept

Experimental Heat Loss Error Propagation in Latent Heat Calculations
Question 117Question

A solid metallic sphere of mass 0.4 kg0.4\text{ kg} and specific heat capacity 500 J kg1 K1500\text{ J kg}^{-1}\text{ K}^{-1} is heated to 100C100^\circ\text{C} and then placed into a well-insulated calorimeter of heat capacity 100 J K1100\text{ J K}^{-1}. The calorimeter contains 0.5 kg0.5\text{ kg} of a liquid initially at 20C20^\circ\text{C}. If the final equilibrium temperature of the system is 40C40^\circ\text{C} and heat loss to the surroundings is negligible, what is the specific heat capacity of the liquid?

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Answer: 1000 J kg1 K11000\text{ J kg}^{-1}\text{ K}^{-1}

Answer

1000 J kg1 K11000\text{ J kg}^{-1}\text{ K}^{-1}
The heat lost by the cooling metallic sphere is Q=0.4×500×60=12000 JQ = 0.4 \times 500 \times 60 = 12000\text{ J}. This energy raises the temperature of both the calorimeter container and the liquid by 20C20^\circ\text{C}. Setting (100+0.5cliquid)×20=12000(100 + 0.5 c_{\text{liquid}}) \times 20 = 12000 yields 100+0.5cliquid=600100 + 0.5 c_{\text{liquid}} = 600, giving cliquid=1000 J kg1 K1c_{\text{liquid}} = 1000\text{ J kg}^{-1}\text{ K}^{-1}.

Step-by-Step Solution

1
Calculate the total heat energy lost by the cooling metallic sphere.
Qlost=m1c1(TinitialTfinal)=0.4×500×(10040)=12000 JQ_{\text{lost}} = m_1 c_1 (T_{\text{initial}} - T_{\text{final}}) = 0.4 \times 500 \times (100 - 40) = 12000\text{ J}
Heat lost depends on mass, specific heat capacity, and temperature decrease of the hot body.
2
Formulate the thermal energy absorption by the calorimeter and liquid.
Qgained=(Ccal+m2c2)(TfinalTinitial, liquid)=(100+0.5c2)×(4020)Q_{\text{gained}} = (C_{\text{cal}} + m_2 c_2) (T_{\text{final}} - T_{\text{initial, liquid}}) = (100 + 0.5 c_2) \times (40 - 20)
Heat capacity of the container (CcalC_{\text{cal}}) is an extensive property already accounting for container mass, whereas specific heat capacity (c2c_2) must be multiplied by liquid mass.
3
Equate heat lost to heat gained using conservation of thermal energy and solve for c2c_2.
12000=(100+0.5c2)×20    600=100+0.5c2    0.5c2=500    c2=1000 J kg1 K112000 = (100 + 0.5 c_2) \times 20 \implies 600 = 100 + 0.5 c_2 \implies 0.5 c_2 = 500 \implies c_2 = 1000\text{ J kg}^{-1}\text{ K}^{-1}
Assuming no external losses, energy conservation dictates that thermal energy lost equals thermal energy absorbed.

Key Concept

Method of Mixtures and Distinction Between Heat Capacity and Specific Heat Capacity
Question 118Question

A closed rigid container holds a mixture of dry air and water vapour at a temperature of 27C27^\circ\text{C} under a total pressure of 740 mmHg740\text{ mmHg}. The relative humidity of the air inside the container is 80%80\%, and the saturated vapour pressure of water at 27C27^\circ\text{C} is 25 mmHg25\text{ mmHg}. If the container is heated at constant volume to 127C127^\circ\text{C}, what is the partial pressure of the dry air in mmHg\text{mmHg} at this higher temperature?

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Answer: 960

Answer

The partial pressure of dry air inside the container at 127C127^\circ\text{C} is 960 mmHg960\text{ mmHg}.
First, the partial pressure of water vapour at 27C27^\circ\text{C} is determined by multiplying relative humidity (80%80\%) by the saturated vapour pressure (25 mmHg25\text{ mmHg}), yielding 20 mmHg20\text{ mmHg}. Next, subtracting this vapour pressure from the total pressure of 740 mmHg740\text{ mmHg} gives the partial pressure of dry air alone as 720 mmHg720\text{ mmHg} at 27C27^\circ\text{C} (300 K300\text{ K}). Finally, applying the Pressure Law (P1T1=P2T2\frac{P_1}{T_1} = \frac{P_2}{T_2}) for the dry air between 300 K300\text{ K} and 400 K400\text{ K} (127C127^\circ\text{C}) yields P2=720×400300=960 mmHgP_2 = 720 \times \frac{400}{300} = 960\text{ mmHg}.

Step-by-Step Solution

1
Calculate the partial pressure of water vapour at 27C27^\circ\text{C}
Pvapour,1=0.80×25 mmHg=20 mmHgP_{\text{vapour}, 1} = 0.80 \times 25\text{ mmHg} = 20\text{ mmHg}
Relative humidity is the ratio of actual partial vapour pressure to the saturated vapour pressure at that temperature.
2
Determine the initial partial pressure of the dry air at 27C27^\circ\text{C} using Dalton's Law
Pdry air,1=740 mmHg20 mmHg=720 mmHgP_{\text{dry air}, 1} = 740\text{ mmHg} - 20\text{ mmHg} = 720\text{ mmHg}
Total pressure of a gas mixture is the sum of the partial pressures of its individual components.
3
Convert temperatures to Kelvin and apply Gay-Lussac's Pressure Law for dry air at constant volume
T1=27+273=300 KT_1 = 27 + 273 = 300\text{ K}, T2=127+273=400 KT_2 = 127 + 273 = 400\text{ K}. Pdry air,2=720 mmHg×(400 K300 K)=960 mmHgP_{\text{dry air}, 2} = 720\text{ mmHg} \times \left(\frac{400\text{ K}}{300\text{ K}}\right) = 960\text{ mmHg}
For a fixed mass of gas at constant volume, pressure is directly proportional to absolute temperature.

Key Concept

Dalton's Law of Partial Pressures and Gay-Lussac's Pressure Law applied to gas-vapour mixtures
Question 119Question

A metal block of mass 4.0 kg4.0\text{ kg} absorbs 12 kJ12\text{ kJ} of thermal energy, causing its temperature to rise by 15 K15\text{ K}. What is the specific heat capacity of the metal block in J kg1K1\text{J kg}^{-1}\text{K}^{-1}?

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Answer: 200

Answer

The specific heat capacity of the metal block is 200 J kg1K1200\text{ J kg}^{-1}\text{K}^{-1}.
Specific heat capacity cc is determined using c=QmΔTc = \frac{Q}{m \Delta T}. Substituting Q=12,000 JQ = 12,000\text{ J}, m=4.0 kgm = 4.0\text{ kg}, and ΔT=15 K\Delta T = 15\text{ K} yields c=120004.0×15=200 J kg1K1c = \frac{12000}{4.0 \times 15} = 200\text{ J kg}^{-1}\text{K}^{-1}.

Step-by-Step Solution

1
Convert given energy to standard SI units
Q=12 kJ=12,000 JQ = 12\text{ kJ} = 12,000\text{ J}
Calculation of specific heat capacity requires heat energy in Joules.
2
Relate heat energy, mass, specific heat capacity, and temperature change
Q=mcΔT    c=QmΔTQ = m c \Delta T \implies c = \frac{Q}{m \Delta T}
Specific heat capacity cc represents heat energy per unit mass per Kelvin temperature change.
3
Substitute the values and compute the result
c=120004.0×15=200 J kg1K1c = \frac{12000}{4.0 \times 15} = 200\text{ J kg}^{-1}\text{K}^{-1}
Evaluating the expression gives 200 J kg1K1200\text{ J kg}^{-1}\text{K}^{-1}.

Key Concept

Specific heat capacity is the quantity of heat required to raise the temperature of 1 kg1\text{ kg} of a substance by 1 K1\text{ K}, expressed as c=QmΔTc = \frac{Q}{m \Delta T}.
Question 120Question

A sealed room with a volume of 50 m350\text{ m}^3 at a temperature of 20C20^\circ\text{C} contains 0.40 kg0.40\text{ kg} of water vapour. If the mass of water vapour required to saturate 1 m31\text{ m}^3 of air at 20C20^\circ\text{C} is 0.016 kg0.016\text{ kg}, what is the relative humidity of the air in the room?

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Answer: 50%50\%

Answer

50%50\%
Relative humidity is defined as the ratio of the actual mass of water vapour present in a given volume of air to the mass of water vapour required to saturate the same volume at the same temperature. For 50 m350\text{ m}^3 of air, the mass needed for saturation is 50 m3×0.016 kg/m3=0.80 kg50\text{ m}^3 \times 0.016\text{ kg/m}^3 = 0.80\text{ kg}. Dividing the actual mass (0.40 kg0.40\text{ kg}) by 0.80 kg0.80\text{ kg} and multiplying by 100%100\% gives 50%50\%.

Step-by-Step Solution

1
Calculate the total mass of water vapour required to saturate the entire room volume.
Total saturation mass=50 m3×0.016 kg/m3=0.80 kg\text{Total saturation mass} = 50\text{ m}^3 \times 0.016\text{ kg/m}^3 = 0.80\text{ kg}
The saturation density gives the maximum water vapour 1 m31\text{ m}^3 can hold, so it must be scaled by the room volume.
2
Apply the formula for relative humidity.
Relative Humidity=(Actual mass of water vapourSaturation mass of water vapour)×100%\text{Relative Humidity} = \left(\frac{\text{Actual mass of water vapour}}{\text{Saturation mass of water vapour}}\right) \times 100\%
Relative humidity measures the degree of saturation of an air sample at a specific temperature.
3
Substitute the known values to find the relative humidity.
Relative Humidity=(0.40 kg0.80 kg)×100%=50%\text{Relative Humidity} = \left(\frac{0.40\text{ kg}}{0.80\text{ kg}}\right) \times 100\% = 50\%
Simplifying the fraction 0.400.80=0.5\frac{0.40}{0.80} = 0.5, which equals 50%50\%.

Key Concept

Relative Humidity
Estimated Time:1m 15s
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