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CBSE - Class 11 Physics Thermal Properties of Matter Worksheet

EXERCISES

1.
A brass boiler has a base area of 0.15 $m^2$ and thickness 1.0 cm. It boils water at the rate of 6.0 kg/min when placed on a gas stove. Estimate the temperature of the part of the flame in contact with the boiler. Thermal conductivity of brass = $109 J s^{-1} m^{-1} K^{-1}$ ; Heat of vaporisation of water = $2256 \times 10^3 J kg^{-1}$.
2.
Answer the following : (a) The triple-point of water is a standard fixed point in modern thermometry. Why ? What is wrong in taking the melting point of ice and the boiling point of water as standard fixed points (as was originally done in the Celsius scale) ?
3.
The coefficient of volume expansion of glycerine is $49 \times 10^{-5} K^{-1}$. What is the fractional change in its density for a 30 °C rise in temperature ?
4.
The electrical resistance in ohms of a certain thermometer varies with temperature according to the approximate law : $R = R_o [1 + \alpha (T – T_o )]$. The resistance is 101.6 $\Omega$ at the triple-point of water 273.16 K, and 165.5 $\Omega$ at the normal melting point of lead (600.5 K). What is the temperature when the resistance is 123.4 $\Omega$ ?
5.
A 10 kW drilling machine is used to drill a bore in a small aluminium block of mass 8.0 kg. How much is the rise in temperature of the block in 2.5 minutes, assuming 50% of power is used up in heating the machine itself or lost to the surroundings. Specific heat of aluminium = 0.91 J g^{-1} K^{-1}.
6.
A steel tape 1m long is correctly calibrated for a temperature of 27.0 °C. The length of a steel rod measured by this tape is found to be 63.0 cm on a hot day when the temperature is 45.0 °C. What is the actual length of the steel rod on that day ? What is the length of the same steel rod on a day when the temperature is 27.0 °C ? Coefficient of linear expansion of steel = $1.20 \times 10^{-5} K^{-1}$.
7.
A ‘thermacole’ icebox is a cheap and an efficient method for storing small quantities of cooked food in summer in particular. A cubical icebox of side 30 cm has a thickness of 5.0 cm. If 4.0 kg of ice is put in the box, estimate the amount of ice remaining after 6 h. The outside temperature is 45 °C, and co-efficient of thermal conductivity of thermacole is $0.01 J s^{-1} m^{-1} K^{-1}$. [Heat of fusion of water = $335 \times 10^3 J kg^{-1}$]
8.
Explain why :
(d) the earth without its atmosphere would be inhospitably cold
9.
A steel tape 1m long is correctly calibrated for a temperature of 27.0 °C. The length of a steel rod measured by this tape is found to be 63.0 cm on a hot day when the temperature is 45.0 °C. What is the actual length of the steel rod on that day ? What is the length of the same steel rod on a day when the temperature is 27.0 °C ? Coefficient of linear expansion of steel = (1.20 \times 10^{-5}) K^{-1} .
10.
The coefficient of volume expansion of glycerine is (49 \times 10^{-5}) K^{-1}. What is the fractional change in its density for a 30 °C rise in temperature ?
11.
The electrical resistance in ohms of a certain thermometer varies with temperature according to the approximate law :
(R = R_o [1 + \alpha (T – T_o )])
The resistance is 101.6 Ω at the triple-point of water 273.16 K, and 165.5 Ω at the normal melting point of lead (600.5 K). What is the temperature when the resistance is 123.4 Ω ?
12.
A body cools from 80 °C to 50 °C in 5 minutes. Calculate the time it takes to cool from 60 °C to 30 °C. The temperature of the surroundings is 20 °C.
13.
A ‘thermacole’ icebox is a cheap and an efficient method for storing small quantities of cooked food in summer in particular. A cubical icebox of side 30 cm has a thickness of 5.0 cm. If 4.0 kg of ice is put in the box, estimate the amount of ice remaining after 6 h. The outside temperature is 45 °C, and co-efficient of thermal conductivity of thermacole is 0.01 J s^{-1} m^{-1} K^{-1}. [Heat of fusion of water = (335 \times 10^{3}) J kg^{-1}]
14.
A large steel wheel is to be fitted on to a shaft of the same material. At 27 °C, the outer diameter of the shaft is 8.70 cm and the diameter of the central hole in the wheel is 8.69 cm. The shaft is cooled using ‘dry ice’. At what temperature of the shaft does the wheel slip on the shaft? Assume coefficient of linear expansion of the steel to be constant over the required temperature range : (\alpha_{steel} = 1.20 \times 10^{-5}) K^{-1}.
15.
A brass boiler has a base area of 0.15 m^{2} and thickness 1.0 cm. It boils water at the rate of 6.0 kg/min when placed on a gas stove. Estimate the temperature of the part of the flame in contact with the boiler. Thermal conductivity of brass = 109 J s^{-1} m^{-1} K^{-1} ; Heat of vaporisation of water = (2256 \times 10^{3}) J kg^{-1}.
16.
In an experiment on the specific heat of a metal, a 0.20 kg block of the metal at 150 °C is dropped in a copper calorimeter (of water equivalent 0.025 kg) containing 150 $cm^3$ of water at 27 °C. The final temperature is 40 °C. Compute the specific heat of the metal. If heat losses to the surroundings are not negligible, is your answer greater or smaller than the actual value for specific heat of the metal ?
17.
Answer the following : (c) The absolute temperature (Kelvin scale) $T$ is related to the temperature $t_c$ on the Celsius scale by $t_c = T – 273.15$. Why do we have 273.15 in this relation, and not 273.16 ?
18.
Explain why : (e) heating systems based on circulation of steam are more efficient in warming a building than those based on circulation of hot water
19.
A 10 kW drilling machine is used to drill a bore in a small aluminium block of mass 8.0 kg. How much is the rise in temperature of the block in 2.5 minutes, assuming 50% of power is used up in heating the machine itself or lost to the surroundings. Specific heat of aluminium = $0.91 J g^{-1} K^{-1}$.
20.

Two ideal gas thermometers A and B use oxygen and hydrogen respectively. The following observations are made :

(b) What do you think is the reason behind the slight difference in answers of thermometers A and B ? (The thermometers are not faulty). What further procedure is needed in the experiment to reduce the discrepancy between the two readings ?

Worksheet Answers

Solution:

Step 1: Given Variables & Physical Constants

  • Base area of the boiler ($A$): $0.15 \, \text{m}^2$
  • Thickness of the boiler ($d$): $1.0 \, \text{cm} = 1.0 \times 10^{-2} \, \text{m}$
  • Rate of boiling water ($\frac{dm}{dt}$): $6.0 \, \text{kg/min} = \frac{6.0}{60} \, \text{kg/s} = 0.1 \, \text{kg/s}$
  • Thermal conductivity of brass ($K$): $109 \, \text{J s}^{-1} \text{m}^{-1} \text{K}^{-1}$
  • Latent heat of vaporisation of water ($L$): $2256 \times 10^3 \, \text{J/kg}$
  • Temperature of boiling water ($T_2$): $100^\circ\text{C} = 373 \, \text{K}$ [Since water boils at $100^\circ\text{C}$ at atmospheric pressure]

Step 2: Determining the Rate of Heat Flow

The rate of heat transfer ($Q/t$) required to vaporize water at a steady rate is given by the product of the mass flow rate and the latent heat of vaporization [Per the principle of calorimetry]:

$\frac{Q}{t} = \left( \frac{dm}{dt} \right) \times L$

$\frac{Q}{t} = 0.1 \, \text{kg/s} \times 2256 \times 10^3 \, \text{J/kg} = 225,600 \, \text{J/s (or Watts)}$

Step 3: Applying Fourier’s Law of Heat Conduction

The heat transfer rate through a slab of material is governed by the conduction equation [Fourier's Law of Heat Conduction]:

$\frac{Q}{t} = \frac{K \cdot A \cdot (T_1 - T_2)}{d}$

Where $T_1$ is the temperature of the flame side and $T_2$ is the temperature of the water side.

Brass Plate (Thickness d) Flame (T1) Water (T2) Heat Flow Rate: Q/t

Step 4: Algebraic Derivation for Flame Temperature ($T_1$)

Rearranging the equation to solve for $T_1$:

$T_1 - T_2 = \frac{(\frac{Q}{t}) \cdot d}{K \cdot A}$

$T_1 = T_2 + \frac{(\frac{Q}{t}) \cdot d}{K \cdot A}$

Substituting the known values:

$T_1 = 373 + \frac{225,600 \times 1.0 \times 10^{-2}}{109 \times 0.15}$

$T_1 = 373 + \frac{2256}{16.35}$

$T_1 \approx 373 + 137.98$

$T_1 \approx 510.98 \, \text{K}$

Step 5: Conversion to Celsius

Converting back to Celsius [Scale conversion $T(^\circ\text{C}) = T(\text{K}) - 273.15$]:

$T_1 (^\circ\text{C}) \approx 510.98 - 273 = 237.98^\circ\text{C}$

Rounding to significant figures, we obtain $238^\circ\text{C}$.

Final Solution: The estimated temperature of the flame in contact with the boiler is approximately 511 K or 238°C.

Solution:

1. Analysis of the Triple Point of Water

The triple point of water is defined as the unique state where water coexists in three phases—solid (ice), liquid (water), and gas (water vapor)—in thermodynamic equilibrium. Its value is internationally fixed at $273.16 \, K$.

Justification for Selection:

  • Uniqueness: Per the Gibbs Phase Rule ($F = C - P + 2$), the triple point occurs at a specific, invariant temperature and pressure. For water ($C=1$), at $P=3$ phases, the degree of freedom ($F$) is $0$. This ensures the point is unique and reproducible across all laboratories globally.
  • Precision: Unlike phase transitions that occur over a temperature range due to impurity sensitivity, the triple point is a singular point on the $P-T$ phase diagram.
T P Triple Point Solid Vapor Liquid

2. Critical Analysis of Original Fixed Points

The original Celsius scale utilized the melting point of ice ($0^\circ C$) and the boiling point of water ($100^\circ C$) as standard fixed points. This methodology possesses inherent physical drawbacks:

Variable Impact on Melting/Boiling Point
Pressure Dependence The boiling point of water is extremely sensitive to atmospheric pressure fluctuations. A change of $1 \, kPa$ alters the boiling point by approximately $0.3 \, K$. [Per the Clausius-Clapeyron Relation: $\frac{dP}{dT} = \frac{L}{T(V_v - V_l)}$].
Purity Constraints The melting point of ice is affected by dissolved impurities and atmospheric gases. Small concentrations of solutes cause "freezing point depression," leading to non-reproducibility.

3. Logical Conclusion

The adoption of the triple point of water as a single fixed point—in conjunction with the value of the Boltzmann constant—obviates the need for a second reference point. It eliminates the experimental uncertainties introduced by pressure variations and chemical impurities that rendered the two-point system (freezing and boiling) unreliable for modern high-precision metrology.

Final Solution: The triple point of water is chosen because it represents a unique, invariant state of matter defined by fixed pressure and temperature, independent of experimental fluctuations. Conversely, the melting and boiling points are unsuitable as primary standards because they are highly dependent on external pressure and the purity of the substance, leading to lack of international reproducibility.

Solution:

Given Variables & Initial Setup

To determine the fractional change in density of glycerine, we define the following parameters provided in the problem statement:

  • Coefficient of volume expansion of glycerine, $\gamma = 49 \times 10^{-5} \, K^{-1}$
  • Change in temperature, $\Delta T = 30 \, °C = 30 \, K$ [As the magnitude of a temperature interval is identical in Celsius and Kelvin scales].
  • Initial density of glycerine: $\rho_0$
  • Final density of glycerine: $\rho$

Step 1: Establishing the Relationship between Density and Temperature

The volume $V$ of a substance at a temperature $T + \Delta T$ is given by the equation of thermal expansion [Per the definition of the coefficient of volume expansion]:

$V = V_0(1 + \gamma \Delta T)$

Since density $\rho$ is inversely proportional to volume for a fixed mass $m$ ($ \rho = \frac{m}{V} $), the density at the final temperature is:

$\rho = \frac{m}{V} = \frac{m}{V_0(1 + \gamma \Delta T)} = \rho_0(1 + \gamma \Delta T)^{-1}$

Step 2: Applying the Binomial Approximation

Given that the product $\gamma \Delta T$ is very small compared to $1$, we apply the Binomial Theorem $(1 + x)^n \approx 1 + nx$ for $|x| \ll 1$:

$\rho \approx \rho_0(1 - \gamma \Delta T)$

Rearranging this to find the change in density ($\Delta \rho = \rho - \rho_0$):

$\rho - \rho_0 = -\rho_0 \gamma \Delta T$

$\frac{\Delta \rho}{\rho_0} = -\gamma \Delta T$

Step 3: Numerical Calculation

Substitute the known values into the derived expression for fractional change ($\frac{\Delta \rho}{\rho_0}$):

$\text{Fractional change} = -(49 \times 10^{-5} \, K^{-1}) \times (30 \, K)$

$\text{Fractional change} = -(1470 \times 10^{-5})$

$\text{Fractional change} = -1.47 \times 10^{-2}$

Visual Representation of Density Variation

Temperature (T) Density (ρ) ρ₀ ρ

Conclusion on the Negative Sign

The negative sign indicates a decrease in density as temperature increases, which is physically consistent with the expansion of the fluid occupying a larger volume for the same mass [Per the Law of Conservation of Mass].

Final Solution: The fractional change in density is $-1.47 \times 10^{-2}$ (or a decrease of approximately $1.47\%$).

Solution:

Step 1: Given Variables & Initial Setup

The resistance of the thermometer is defined by the linear relation:

$R = R_0 [1 + \alpha (T - T_0)]$

Where:

  • $T_0 = 273.16\text{ K}$ (Triple-point of water)
  • $R_0 = 101.6\text{ }\Omega$ (Resistance at $T_0$)
  • $T_1 = 600.5\text{ K}$ (Normal melting point of lead)
  • $R_1 = 165.5\text{ }\Omega$ (Resistance at $T_1$)
  • $R = 123.4\text{ }\Omega$ (Target resistance)

Step 2: Calculating the Temperature Coefficient ($\alpha$)

Using the values at the melting point of lead, we isolate $\alpha$ [Per the linear resistance-temperature model]:

$165.5 = 101.6 [1 + \alpha (600.5 - 273.16)]$

$\frac{165.5}{101.6} = 1 + \alpha (327.34)$

$1.628937 = 1 + \alpha (327.34)$

$0.628937 = \alpha (327.34)$

$\alpha = \frac{0.628937}{327.34} \approx 1.92135 \times 10^{-3}\text{ K}^{-1}$

Step 3: Solving for Unknown Temperature ($T$)

Using the target resistance $R = 123.4\text{ }\Omega$, we rearrange the initial equation to solve for $T$:

$R = R_0 + R_0 \alpha (T - T_0)$

$T - T_0 = \frac{R - R_0}{R_0 \alpha}$

$T = T_0 + \frac{R - R_0}{R_0 \alpha}$

Substitute the known values:

$T = 273.16 + \frac{123.4 - 101.6}{101.6 \times 1.92135 \times 10^{-3}}$

$T = 273.16 + \frac{21.8}{0.195209}$

$T = 273.16 + 111.675$

$T \approx 384.835\text{ K}$

Visual Representation of Resistance-Temperature Gradient

Temperature (K) Resistance (Ω) 101.6 Ω 123.4 Ω 165.5 Ω

Final Solution: The temperature corresponding to a resistance of 123.4 $\Omega$ is 384.84 K.

Solution:

Step 1: Identifying Given Variables and Constants

  • Power of the drilling machine ($P$): $10\text{ kW} = 10 \times 10^3\text{ W} = 10,000\text{ J/s}$
  • Mass of the aluminium block ($m$): $8.0\text{ kg} = 8,000\text{ g}$
  • Time duration ($\Delta t$): $2.5\text{ minutes} = 2.5 \times 60\text{ s} = 150\text{ s}$
  • Efficiency ($\eta$): $50\% = 0.5$ (fraction of power used for heating)
  • Specific heat capacity of aluminium ($c$): $0.91\text{ J g}^{-1}\text{ K}^{-1}$

Step 2: Calculating Total Energy Generated and Utilized

The total energy ($E_{total}$) produced by the machine is given by the product of power and time [By Definition of Work and Energy, $E = P \times \Delta t$]:

$E_{total} = P \times \Delta t = 10,000\text{ J/s} \times 150\text{ s} = 1,500,000\text{ J}$

Since only $50\%$ of the power is effective in heating the aluminium block ($Q_{absorbed}$):

$Q_{absorbed} = \eta \times E_{total}$

$Q_{absorbed} = 0.5 \times 1,500,000\text{ J} = 750,000\text{ J}$

Step 3: Relating Heat to Temperature Change

The heat energy absorbed by a substance is related to the temperature rise ($\Delta T$) by the formula [Per the Principle of Calorimetry]:

$Q = m \cdot c \cdot \Delta T$

Rearranging the equation to solve for the change in temperature ($\Delta T$):

$\Delta T = \frac{Q_{absorbed}}{m \cdot c}$

Step 4: Algebraic Substitution and Calculation

Substitute the known values into the equation:

$\Delta T = \frac{750,000\text{ J}}{8,000\text{ g} \times 0.91\text{ J g}^{-1}\text{ K}^{-1}}$

$\Delta T = \frac{750,000}{7,280}\text{ K}$

$\Delta T \approx 103.02\text{ K}$

Visual Representation of Thermal Energy Transfer

Aluminium Block (m) Q = 750 kJ T_final = T_initial + ΔT

Final Solution: The rise in temperature of the aluminium block is approximately 103.02 K (or 103.02 °C).

Solution:

Step 1: Given Variables & Parameters

  • Standard temperature ($T_0$): $27.0\ ^\circ\text{C}$
  • Observed temperature ($T$): $45.0\ ^\circ\text{C}$
  • Change in temperature ($\Delta T$): $T - T_0 = 45.0 - 27.0 = 18.0\ \text{K}$ [Since a change in Celsius is equivalent to a change in Kelvin]
  • Coefficient of linear expansion of steel ($\alpha$): $1.20 \times 10^{-5}\ \text{K}^{-1}$
  • Calibrated length of tape ($L_0$): $1.00\ \text{m} = 100\ \text{cm}$
  • Measured length of rod by the tape at $45.0\ ^\circ\text{C}$ ($L_{measured}$): $63.0\ \text{cm}$

Step 2: Calculating the Actual Length of the Rod at 45.0 °C

The steel tape expands at $45.0\ ^\circ\text{C}$. The length of the tape $L'$ corresponding to the $1\ \text{cm}$ marking at $T_0$ is given by the linear expansion formula: $L' = L_0(1 + \alpha \Delta T)$.

Therefore, a marking of $1\ \text{cm}$ on the tape at $45.0\ ^\circ\text{C}$ represents an actual length of:

$L_{actual\_unit} = 1 \times (1 + (1.20 \times 10^{-5} \times 18.0))$

$L_{actual\_unit} = 1 + 2.16 \times 10^{-4} = 1.000216\ \text{cm}$

The actual length of the rod ($L_{actual}$) is the measured length multiplied by this factor:

$L_{actual} = 63.0 \times 1.000216 \approx 63.0136\ \text{cm}$

Step 3: Calculating the Length of the Rod at 27.0 °C

The rod, like the tape, also has a coefficient of linear expansion $\alpha$. Let $L_{27}$ be the length of the rod at $27.0\ ^\circ\text{C}$. The length of the rod at $45.0\ ^\circ\text{C}$ ($L_{45}$) relates to its length at $27.0\ ^\circ\text{C}$ by the expansion formula: $L_{45} = L_{27}(1 + \alpha \Delta T)$.

$63.0136 = L_{27}(1 + (1.20 \times 10^{-5} \times 18.0))$

$63.0136 = L_{27}(1.000216)$

$L_{27} = \frac{63.0136}{1.000216} \approx 63.0000\ \text{cm}$

Visual Representation of Thermal Expansion

Steel Tape at 27°C (1m) Expanded Steel Tape at 45°C (1m + ΔL)

Analytical Summary

Condition Calculated Length
Actual length of rod at 45.0 °C 63.0136 cm
Actual length of rod at 27.0 °C 63.0000 cm

Final Solution: The actual length of the rod at 45.0 °C is 63.0136 cm, and the length of the same rod at 27.0 °C is 63.0000 cm.

Solution:

Given Variables & Initial Setup

To determine the mass of ice remaining, we must calculate the total heat energy ($Q$) that flows into the icebox through its walls via thermal conduction over the specified duration.

  • Side of the cubical box ($L$): $0.30 \, m$
  • Thickness of the walls ($\Delta x$): $0.05 \, m$
  • Initial mass of ice ($M_{initial}$): $4.0 \, kg$
  • Time duration ($t$): $6 \, hours = 6 \times 3600 \, s = 21600 \, s$
  • Outside temperature ($T_2$): $45 \, ^\circ C$
  • Inside temperature ($T_1$): $0 \, ^\circ C$ (since ice is present)
  • Temperature difference ($\Delta T$): $45 - 0 = 45 \, K$
  • Thermal conductivity ($K$): $0.01 \, J \, s^{-1} \, m^{-1} \, K^{-1}$
  • Latent heat of fusion of water ($L_f$): $335 \times 10^3 \, J \, kg^{-1}$

Step 1: Calculating Surface Area

A cube has 6 faces. The surface area ($A$) of each face is $L^2$. Therefore, the total surface area for heat transfer is:

$A = 6 \times L^2 = 6 \times (0.30 \, m)^2 = 6 \times 0.09 \, m^2 = 0.54 \, m^2$

Step 2: Determining Total Heat Influx

Per the Fourier Law of Thermal Conduction: $Q = \frac{K \cdot A \cdot \Delta T \cdot t}{\Delta x}$

Substituting the values:

$Q = \frac{0.01 \cdot 0.54 \cdot 45 \cdot 21600}{0.05}$

$Q = \frac{0.243 \times 21600}{0.05} = \frac{5248.8}{0.05} = 104976 \, J$

Step 3: Calculating Mass of Melted Ice

The heat required to melt a mass $m$ of ice is $Q = m \cdot L_f$. Thus, $m = \frac{Q}{L_f}$

$m = \frac{104976}{335 \times 10^3} \, kg$

$m \approx 0.313 \, kg$

Step 4: Final Mass Remaining

$M_{remaining} = M_{initial} - m$

$M_{remaining} = 4.0 - 0.313 = 3.687 \, kg$

30 cm 5 cm thick Heat Flux Q = KAΔT/Δx

Final Solution: The amount of ice remaining after 6 hours is approximately 3.69 kg.

Solution:

1. Theoretical Foundation: The Greenhouse Effect and Radiative Equilibrium

The Earth's surface temperature is determined by a radiative balance between incoming solar radiation (primarily short-wave visible light) and outgoing terrestrial radiation (long-wave infrared radiation). The atmosphere acts as a selective filter, governed by the following physical principles:

  • Stefan-Boltzmann Law: The power radiated by a black body per unit area is proportional to the fourth power of its absolute temperature: $P = \sigma A T^4$ [Where $\sigma = 5.67 \times 10^{-8} \, W m^{-2} K^{-4}$].
  • Wien’s Displacement Law: The wavelength of maximum emission is inversely proportional to temperature: $\lambda_{max} T = b$ [Where $b \approx 2.898 \times 10^{-3} \, m \cdot K$].

2. Interaction of Solar and Terrestrial Radiation

Radiation Type Source Wavelength Atmospheric Interaction
Short-wave Sun (~5800 K) Visible/UV Largely transparent; reaches Earth's surface.
Long-wave Earth (~288 K) Infrared (IR) Absorbed/re-emitted by greenhouse gases ($CO_2, H_2O, CH_4$).

3. Visualizing the Radiative Trap

Earth Surface Solar Input IR Trapped

4. Step-by-Step Analytical Breakdown

Step 1: The Without-Atmosphere Scenario
If the atmosphere were removed, the Earth would function as a bare black body in the vacuum of space. It would absorb solar radiation and emit thermal radiation directly into space without any re-absorption. The effective temperature ($T_e$) would be approximately $255 \, K$ ($-18^\circ C$).

Step 2: The Mechanism of Atmospheric Retention
Greenhouse gases in the atmosphere possess vibrational/rotational energy states that correspond to the frequencies of outgoing infrared (IR) radiation. By absorbing these photons, the atmosphere becomes heated [Per the Principle of Selective Absorption].

Step 3: Back-Radiation
The warmed atmosphere re-radiates a significant portion of this thermal energy back toward the Earth's surface. This "Back-Radiation" adds to the energy flux received from the Sun, raising the equilibrium temperature of the surface to the current global average of approximately $288 \, K$ ($15^\circ C$).

5. Conclusion

Without the atmosphere, the lack of this "radiative insulation" would result in a massive net loss of energy to space. The Earth would not be able to maintain the thermal energy required to sustain liquid water or biological processes, leading to an average surface temperature drop of roughly $33^\circ C$, rendering the planet inhospitable.

Final Solution: The atmosphere traps outgoing infrared radiation through the greenhouse effect, maintaining a surface temperature higher than the radiative equilibrium of a vacuum-exposed Earth; without this insulation, the Earth would radiate heat rapidly into space, resulting in sub-zero temperatures across most of the planet.

Solution:

Given Variables & Initial Setup

  • Calibration temperature of tape ($T_0$): $27.0 \, ^\circ\text{C}$
  • Temperature on the hot day ($T$): $45.0 \, ^\circ\text{C}$
  • Observed length of the rod at $T$ ($L'_{obs}$): $63.0 \, \text{cm}$
  • Coefficient of linear expansion of steel ($\alpha$): $1.20 \times 10^{-5} \, \text{K}^{-1}$

Step 1: Calculating the Thermal Expansion of the Tape

The tape expands as the temperature increases from $27.0 \, ^\circ\text{C}$ to $45.0 \, ^\circ\text{C}$. The change in temperature is $\Delta T = 45.0 - 27.0 = 18.0 \, \text{K}$.

The actual length ($L$) of a scale marking representing $1 \, \text{cm}$ on the tape at the hot day is given by the linear expansion formula [Per the Thermal Expansion Law]:

$L = L_0(1 + \alpha \Delta T)$

$L = 1 \, \text{cm} \times [1 + (1.20 \times 10^{-5} \, \text{K}^{-1})(18.0 \, \text{K})]$

$L = 1 + 2.16 \times 10^{-4} = 1.000216 \, \text{cm}$

Step 2: Determining the Actual Length of the Rod at 45.0 °C

The rod length measured by the tape is $63.0$ markings. Since each marking corresponds to $1.000216 \, \text{cm}$ at $45.0 \, ^\circ\text{C}$, the actual length ($L_{actual, 45}$) is:

$L_{actual, 45} = 63.0 \times 1.000216 \, \text{cm}$

$L_{actual, 45} = 63.013608 \, \text{cm} \approx 63.014 \, \text{cm}$

Step 3: Calculating the Length of the Rod at 27.0 °C

To find the length of the rod at the calibration temperature ($27.0 \, ^\circ\text{C}$), we reverse the thermal expansion of the rod itself using the same coefficient [Per the Law of Thermal Contraction]:

$L_{27} = \frac{L_{actual, 45}}{1 + \alpha \Delta T}$

$L_{27} = \frac{63.013608}{1 + (1.20 \times 10^{-5})(18.0)}$

$L_{27} = \frac{63.013608}{1.000216} = 63.0 \, \text{cm}$

27.0 °C (Standard) Length = 63.0 cm Physical Steel Rod Representation

Summary of Results

Condition Actual Length
At $45.0 \, ^\circ\text{C}$ $63.014 \, \text{cm}$
At $27.0 \, ^\circ\text{C}$ $63.000 \, \text{cm}$

Final Solution: The actual length of the rod at 45.0 °C is 63.014 cm, and at 27.0 °C, it is 63.0 cm.

Solution:

Given Variables & Initial Setup

The following parameters are provided for the substance glycerine:

  • Coefficient of volume expansion ($\gamma$): $49 \times 10^{-5} \, \text{K}^{-1}$
  • Change in temperature ($\Delta T$): $30 \, ^\circ\text{C} = 30 \, \text{K}$

[Per the definition of thermal expansion, the volume of a substance increases as temperature increases, and since mass remains constant, density must decrease.]

Step 1: Derivation of the Relationship between Density and Temperature

The density ($\rho$) of a substance is defined as mass ($m$) divided by volume ($V$):

$\rho = \frac{m}{V}$

For a small change in temperature $\Delta T$, the new volume $V'$ is given by the formula:

$V' = V(1 + \gamma \Delta T)$

The new density $\rho'$ is therefore:

$\rho' = \frac{m}{V'} = \frac{m}{V(1 + \gamma \Delta T)} = \rho(1 + \gamma \Delta T)^{-1}$

[Using the Binomial Theorem $(1 + x)^n \approx 1 + nx$ for small $x$, where $\gamma \Delta T \ll 1$]:

$\rho' \approx \rho(1 - \gamma \Delta T)$

Step 2: Calculating Fractional Change in Density

The fractional change in density is defined as the ratio of the change in density ($\Delta \rho$) to the original density ($\rho$):

$\Delta \rho = \rho' - \rho = \rho(1 - \gamma \Delta T) - \rho = -\rho \gamma \Delta T$

The fractional change is:

$\frac{\Delta \rho}{\rho} = -\gamma \Delta T$

[The negative sign indicates a decrease in density as temperature rises].

Step 3: Numerical Substitution

Substitute the given values into the derived equation:

$\frac{\Delta \rho}{\rho} = -(49 \times 10^{-5} \, \text{K}^{-1}) \times (30 \, \text{K})$

$\frac{\Delta \rho}{\rho} = -(49 \times 30) \times 10^{-5}$

$\frac{\Delta \rho}{\rho} = -1470 \times 10^{-5}$

$\frac{\Delta \rho}{\rho} = -1.47 \times 10^{-2}$

$\frac{\Delta \rho}{\rho} = -0.0147$

Density ($\rho$) vs Temperature ($T$) Relationship T $\rho$

Final Solution: The fractional decrease in the density of glycerine for a 30 °C rise in temperature is $1.47 \times 10^{-2}$ (or approximately $1.47\%$).

Solution:

Step 1: Given Variables & Initial Setup

The relationship between electrical resistance $R$ and temperature $T$ is governed by the linear model:

$R = R_0 [1 + \alpha (T - T_0)]$

From the problem statement, we identify the following data points:

  • Reference Temperature ($T_0$): $273.16\text{ K}$ (Triple point of water)
  • Resistance at $T_0$ ($R_0$): $101.6\text{ }\Omega$
  • Temperature at melting point of lead ($T_1$): $600.5\text{ K}$
  • Resistance at $T_1$ ($R_1$): $165.5\text{ }\Omega$
  • Target Resistance ($R_t$): $123.4\text{ }\Omega$
  • Target Temperature ($T$): To be determined.

Step 2: Determining the Temperature Coefficient ($\alpha$)

Using the linear equation for the known state at the melting point of lead, we isolate the coefficient $\alpha$:

$R_1 = R_0 [1 + \alpha(T_1 - T_0)]$

Substituting the known values:

$165.5 = 101.6 [1 + \alpha(600.5 - 273.16)]$

$165.5 = 101.6 [1 + \alpha(327.34)]$

Divide by $101.6$:

$1.628937 = 1 + \alpha(327.34)$

$0.628937 = \alpha(327.34)$

$\alpha = \frac{0.628937}{327.34} \approx 1.92135 \times 10^{-3}\text{ K}^{-1}$

Step 3: Calculating the Target Temperature ($T$)

We rearrange the original formula to solve for $T$ at $R_t = 123.4\text{ }\Omega$:

$R_t = R_0 [1 + \alpha(T - T_0)]$

$\frac{R_t}{R_0} = 1 + \alpha(T - T_0)$

$\frac{R_t}{R_0} - 1 = \alpha(T - T_0)$

$T = T_0 + \frac{R_t - R_0}{\alpha \cdot R_0}$

Substituting the values:

$T = 273.16 + \frac{123.4 - 101.6}{(1.92135 \times 10^{-3}) \times 101.6}$

$T = 273.16 + \frac{21.8}{0.195209}$

$T = 273.16 + 111.675$

$T \approx 384.835\text{ K}$

Visual Representation of Linear Resistance Model

Temperature (K) Resistance (Ω) 101.6 165.5

Final Solution: The temperature when the resistance is 123.4 Ω is approximately 384.84 K.

Solution:

Given Variables & Initial Setup

According to Newton’s Law of Cooling, the rate of loss of heat is directly proportional to the difference in temperature between the body and its surroundings, provided the difference is small. The formula is expressed as:

$$\frac{dT}{dt} = -K(T - T_s)$$

Where:

  • $T$ = Temperature of the body
  • $T_s$ = Temperature of the surroundings = $20^\circ\text{C}$
  • $K$ = Positive constant
  • $t$ = Time

For finite temperature differences, we use the integrated form (average temperature approximation):

$$\frac{T_1 - T_2}{t} = K\left(\frac{T_1 + T_2}{2} - T_s\right)$$

Step 1: Analyzing the First Cooling Interval

Interval: $80^\circ\text{C}$ to $50^\circ\text{C}$ in $t_1 = 5$ minutes.

Substituting the values into the cooling formula:

$$\frac{80 - 50}{5} = K\left(\frac{80 + 50}{2} - 20\right)$$

$$\frac{30}{5} = K(65 - 20)$$

$$6 = K(45) \implies K = \frac{6}{45} = \frac{2}{15} \text{ min}^{-1}$$

[Justification: Per Newton's Law of Cooling applied to the interval mean temperature.]

Step 2: Analyzing the Second Cooling Interval

Interval: $60^\circ\text{C}$ to $30^\circ\text{C}$ in time $t_2$.

Using the constant $K$ derived in Step 1:

$$\frac{60 - 30}{t_2} = K\left(\frac{60 + 30}{2} - 20\right)$$

$$\frac{30}{t_2} = \left(\frac{2}{15}\right)(45 - 20)$$

$$\frac{30}{t_2} = \left(\frac{2}{15}\right)(25)$$

$$\frac{30}{t_2} = \frac{50}{15} = \frac{10}{3}$$

Step 3: Calculating Final Time

Solving for $t_2$:

$$t_2 = \frac{30 \times 3}{10}$$

$$t_2 = 9 \text{ minutes}$$

Visual Representation of Cooling Curve

Time (min) Temperature (°C) 80°C 20°C (Ts)

Final Solution: The time taken to cool from 60 °C to 30 °C is 9 minutes.

Solution:

Step 1: Identifying Given Variables

  • Side of the cube ($l$): $30\text{ cm} = 0.3\text{ m}$
  • Thickness of thermacole ($\Delta x$): $5.0\text{ cm} = 0.05\text{ m}$
  • Mass of ice ($m_{initial}$): $4.0\text{ kg}$
  • Time duration ($t$): $6\text{ h} = 6 \times 3600\text{ s} = 21,600\text{ s}$
  • Temperature difference ($\Delta T$): $T_{outside} - T_{inside} = 45^\circ\text{C} - 0^\circ\text{C} = 45\text{ K}$
  • Thermal conductivity ($K$): $0.01\text{ J s}^{-1}\text{ m}^{-1}\text{ K}^{-1}$
  • Latent heat of fusion of ice ($L_f$): $335 \times 10^3\text{ J kg}^{-1}$

Step 2: Calculating Surface Area for Heat Transfer

A cube has 6 faces. The total surface area ($A$) is:

$A = 6 \times l^2 = 6 \times (0.3\text{ m})^2 = 6 \times 0.09\text{ m}^2 = 0.54\text{ m}^2$ [Per the definition of geometric surface area for a cube] Icebox (30cm) Area A = 0.54 m²

Step 3: Calculating Total Heat Conducted ($Q$)

Using the steady-state heat conduction formula [Fourier’s Law of Heat Conduction]:

$Q = \frac{K \cdot A \cdot \Delta T \cdot t}{\Delta x}$ $Q = \frac{0.01 \cdot 0.54 \cdot 45 \cdot 21600}{0.05}$ $Q = \frac{5248.8}{0.05} = 104,976\text{ J}$

Step 4: Calculating Mass of Ice Melted ($m_{melted}$)**

The heat absorbed causes the ice to change state at constant temperature ($0^\circ\text{C}$). [Per the Principle of Latent Heat]

$Q = m_{melted} \cdot L_f$ $m_{melted} = \frac{Q}{L_f}$ $m_{melted} = \frac{104,976}{335 \times 10^3} \approx 0.313\text{ kg}$

Step 5: Determining Remaining Ice

$m_{remaining} = m_{initial} - m_{melted}$ $m_{remaining} = 4.0\text{ kg} - 0.313\text{ kg} = 3.687\text{ kg}$

Final Solution: The estimated amount of ice remaining after 6 hours is approximately 3.69 kg.

Solution:

Given Variables & Initial Setup

  • Initial temperature $T_1 = 27\,^\circ\text{C} = 300\,\text{K}$
  • Initial diameter of shaft $D_s = 8.70\,\text{cm}$
  • Initial diameter of hole $D_h = 8.69\,\text{cm}$
  • Coefficient of linear expansion $\alpha = 1.20 \times 10^{-5}\,\text{K}^{-1}$

To fit the wheel onto the shaft, the shaft must be cooled until its diameter $D_s'$ is equal to the diameter of the hole $D_h$. Since the coefficient of linear expansion is assumed constant, we utilize the linear thermal expansion formula: $D' = D(1 + \alpha \Delta T)$ [Per the definition of thermal expansion].

Step 1: Formulating the Thermal Contraction Equation

The shaft diameter must reduce from $8.70\,\text{cm}$ to $8.69\,\text{cm}$. Let $T_2$ be the final temperature of the shaft. The change in length is governed by:

$D_h = D_s[1 + \alpha(T_2 - T_1)]$

Step 2: Algebraic Manipulation and Solving for $\Delta T$

Rearranging the equation to isolate the change in temperature $\Delta T = (T_2 - T_1)$:

$\frac{D_h}{D_s} = 1 + \alpha \Delta T$

$\alpha \Delta T = \frac{D_h}{D_s} - 1$

$\Delta T = \frac{D_h - D_s}{D_s \cdot \alpha}$

Step 3: Numerical Calculation

Substitute the given values into the derived expression:

$\Delta T = \frac{8.69 - 8.70}{8.70 \times 1.20 \times 10^{-5}}$

$\Delta T = \frac{-0.01}{8.70 \times 1.20 \times 10^{-5}}$

$\Delta T = \frac{-0.01}{1.044 \times 10^{-4}}$

$\Delta T \approx -95.78\,\text{K}$

Step 4: Determining Final Temperature

Since $\Delta T = T_2 - T_1$:

$T_2 = T_1 + \Delta T$

$T_2 = 27\,^\circ\text{C} - 95.78\,^\circ\text{C}$

$T_2 \approx -68.78\,^\circ\text{C}$

Shaft at 27°C Cooling (-95.8 K) Shaft at -68.8°C

Final Solution: The shaft must be cooled to approximately -68.8 °C to fit the wheel.

Solution:

Step 1: Given Variables & Initial Setup

To determine the temperature of the flame, we equate the heat conducted through the brass boiler to the heat absorbed by the water for phase change.

  • Base area ($A$) = $0.15 \, \text{m}^2$
  • Thickness ($\Delta x$) = $1.0 \, \text{cm} = 0.01 \, \text{m}$
  • Rate of boiling ($dm/dt$) = $6.0 \, \text{kg/min} = \frac{6.0}{60} \, \text{kg/s} = 0.1 \, \text{kg/s}$
  • Thermal conductivity of brass ($K$) = $109 \, \text{J s}^{-1} \text{m}^{-1} \text{K}^{-1}$
  • Latent heat of vaporisation ($L_v$) = $2256 \times 10^3 \, \text{J/kg}$
  • Temperature of boiling water ($T_2$) = $100^\circ\text{C} = 373 \, \text{K}$

Step 2: Formulating the Energy Balance

The rate of heat transfer ($Q/t$) via conduction is given by Fourier's Law of Heat Conduction [Per Fourier’s Law]:

$\frac{Q}{t} = \frac{K \cdot A \cdot (T_1 - T_2)}{\Delta x}$

The rate of heat required for boiling water is given by:

$\frac{Q}{t} = L_v \cdot \frac{dm}{dt}$

Step 3: Algebraic Derivation for $T_1$

Equating the two expressions:

$L_v \cdot \frac{dm}{dt} = \frac{K \cdot A \cdot (T_1 - T_2)}{\Delta x}$

Rearranging to solve for $T_1$ (the temperature of the flame):

$T_1 = T_2 + \frac{L_v \cdot (dm/dt) \cdot \Delta x}{K \cdot A}$

Step 4: Calculation

Substitute the values into the derived equation:

$T_1 = 373 + \frac{(2256 \times 10^3) \cdot (0.1) \cdot (0.01)}{109 \cdot 0.15}$

$T_1 = 373 + \frac{2256}{16.35}$

$T_1 = 373 + 137.98$

$T_1 \approx 510.98 \, \text{K}$

Visual Representation of Thermal Flux

Brass Boiler Base (Thickness = 0.01m) Conductivity (K) = 109 W/mK Heat Flow (Q/t) Flame Temperature (T1 = 511 K) Boiling Water (T2 = 373 K)

Step 5: Final Conversion

Convert temperature from Kelvin back to Celsius if required by context, though Kelvin is the standard SI unit for thermal calculations:

$T_{^\circ\text{C}} = 510.98 - 273.15 = 237.83^\circ\text{C}$

Final Solution: The temperature of the flame in contact with the boiler is approximately 511 K or 237.8 °C.

Solution:

Step 1: Identifying Given Variables

Mass of the metal block ($m_m$) = $0.20\text{ kg}$

Initial temperature of the metal ($T_m$) = $150\text{ °C}$

Water equivalent of the calorimeter ($W$) = $0.025\text{ kg}$

Volume of water ($V_w$) = $150\text{ cm}^3 \Rightarrow$ Mass of water ($m_w$) = $0.150\text{ kg}$ [Since density $\rho = 1\text{ g/cm}^3$]

Initial temperature of water and calorimeter ($T_i$) = $27\text{ °C}$

Final equilibrium temperature ($T_f$) = $40\text{ °C}$

Specific heat capacity of water ($c_w$) = $4186\text{ J kg}^{-1}\text{ K}^{-1}$

Step 2: Theoretical Framework: Principle of Calorimetry

Per the Principle of Calorimetry: Heat lost by the hot body = Heat gained by the cold body system.

$\Delta Q_{\text{lost}} = \Delta Q_{\text{gained}}$

$m_m \cdot c_m \cdot (T_m - T_f) = (m_w \cdot c_w + W \cdot c_w) \cdot (T_f - T_i)$

[Note: $W$ represents the mass of water that would have the same heat capacity as the calorimeter; hence, it adds to the thermal mass of the water.]

Step 3: Algebraic Calculation

Substitute the known values into the equation:

$0.20 \cdot c_m \cdot (150 - 40) = (0.150 + 0.025) \cdot 4186 \cdot (40 - 27)$

$0.20 \cdot c_m \cdot 110 = 0.175 \cdot 4186 \cdot 13$

$22 \cdot c_m = 9523.15$

$c_m = \frac{9523.15}{22} \approx 432.87\text{ J kg}^{-1}\text{ K}^{-1}$

Step 4: Analyzing Heat Loss to Surroundings

If heat losses to the surroundings were not negligible, the measured $T_f$ (40 °C) would be lower than the theoretical equilibrium temperature achieved in an adiabatic system.

Looking at the heat balance equation: $c_m = \frac{(m_w + W) \cdot c_w \cdot (T_f - T_i)}{m_m \cdot (T_m - T_f)}$.

If $T_f$ is smaller than the true value, the numerator $(T_f - T_i)$ decreases and the denominator $(T_m - T_f)$ increases. Consequently, the calculated specific heat value would be smaller than the actual value.

Time / Process Progression Temperature T_m = 150°C T_f = 40°C

Final Solution: The specific heat of the metal is approximately $432.87\text{ J kg}^{-1}\text{ K}^{-1}$. If heat losses were considered, the calculated value would be smaller than the actual value.

Solution:

Step 1: Theoretical Basis of the Thermodynamic Scale

The Kelvin scale, also known as the absolute thermodynamic temperature scale, is defined based on the behavior of ideal gases and the triple point of water. Historically, the scale was tied to two fixed points: absolute zero (where the pressure of an ideal gas extrapolated to zero) and the triple point of water (the unique temperature and pressure at which ice, liquid water, and water vapor coexist in equilibrium). [Per the International System of Units (SI) standards].

Step 2: Defining the Triple Point of Water

By international agreement, the triple point of water is assigned an exact numerical value of $273.16 \, \text{K}$. This selection serves as the fundamental fixed point for defining the magnitude of the Kelvin unit. The relationship is defined as:

$T_{tp} = 273.16 \, \text{K}$

Step 3: Defining the Celsius Scale Relative to the Triple Point

The Celsius scale is defined such that the freezing point of water (at standard atmospheric pressure, $1 \, \text{atm}$) is $0 \, ^\circ\text{C}$, and the boiling point of water is $100 \, ^\circ\text{C}$. Experimental measurements indicate that the freezing point of water (ice point) at $1 \, \text{atm}$ is approximately $0.01 \, ^\circ\text{C}$ lower than the triple point of water.

Mathematically:

$t_{ice} \approx T_{tp} - 273.15$

$0 \, ^\circ\text{C} = 273.16 \, \text{K} - 273.15 \, \text{K}$

Step 4: Logical Comparison of the Constants

Parameter Value (K) Significance
Triple Point of Water $273.16$ Fundamental reference point defined by SI.
Ice Point (at $1 \, \text{atm}$) $273.15$ Practical reference point relative to $0 \, ^\circ\text{C}$.

If we used $273.16$ in the conversion formula $t_c = T - 273.16$, the freezing point of water would occur at $0 \, \text{K}$ (which is absolute zero), which is physically impossible as the ice point is at $273.15 \, \text{K}$. Therefore, $273.15$ is the necessary offset to align the Celsius scale's zero point with the physical freezing point of water at $1 \, \text{atm}$ while maintaining the Kelvin scale's definition centered on the $273.16 \, \text{K}$ triple point.

Visual Representation of Scale Alignment

0 K 273.15 K 273.16 K 0 °C 0.01 °C

Final Solution: The constant 273.16 is the defined absolute temperature of the triple point of water. The constant 273.15 is used in the conversion formula $t_c = T - 273.15$ because the freezing point of water at 1 atm is 0.01 K lower than the triple point of water, ensuring that 0 °C correctly corresponds to 273.15 K.

Solution:

Theoretical Foundation: Latent Heat vs. Specific Heat

To analyze the efficiency of heating systems, we must compare the energy transfer mechanisms of water at $100^\circ\text{C}$ and steam at $100^\circ\text{C}$.

  • Hot Water Heating: Relies primarily on the specific heat capacity of water. As water cools from $100^\circ\text{C}$ to room temperature ($T_r$), the heat released ($Q_w$) is defined by: $Q_w = m \cdot c_w \cdot (100 - T_r)$, where $c_w \approx 4186 \, \text{J/kg}\cdot\text{K}$.
  • Steam Heating: Utilizes both the latent heat of vaporization and the specific heat of condensed water. Steam first releases its latent heat at $100^\circ\text{C}$, followed by the cooling of the resulting water. The heat released ($Q_s$) is: $Q_s = m \cdot L_v + m \cdot c_w \cdot (100 - T_r)$, where $L_v \approx 22.6 \times 10^5 \, \text{J/kg}$.

Step 1: Quantitative Comparison of Heat Energy

Consider $1 \, \text{kg}$ of substance at $100^\circ\text{C}$ transferring heat to a room at $20^\circ\text{C}$.

Mechanism Calculation Total Energy Released
Hot Water $1 \cdot 4186 \cdot (100 - 20)$ $334,880 \, \text{J}$
Steam $(1 \cdot 22.6 \times 10^5) + (1 \cdot 4186 \cdot 80)$ $2,594,880 \, \text{J}$

[Per the Principle of Calorimetry, $Q_{total} = \sum mc\Delta T + \sum mL$].

Step 2: Analysis of Heat Transfer Efficiency

The steam system is significantly more efficient because the latent heat of vaporization ($L_v$) is an order of magnitude larger than the sensible heat released by water cooling over a standard temperature range.
When steam comes into contact with the cooler radiator surfaces, it undergoes a phase change (condensation), releasing a massive amount of energy ($2.26 \times 10^6 \, \text{J/kg}$) isothermally at $100^\circ\text{C}$.

Visual Representation of Phase Energy

Heat Added/Removed Temperature Latent Heat Release (Phase Change) Sensible Heat

Step 3: Conclusion on System Performance

Because steam provides a much higher energy density per unit mass compared to hot water, a steam-based system requires a lower mass-flow rate of fluid to achieve the same heating effect. This leads to smaller pipe sizes, reduced pumping requirements, and higher overall thermodynamic efficiency in large-scale building heating applications.

Final Solution: Steam is more efficient because it releases latent heat of vaporization ($22.6 \times 10^5 \, \text{J/kg}$) in addition to the sensible heat released by the condensed water, providing substantially more thermal energy per kilogram than hot water.

Solution:

Step 1: Given Variables & Initial Parameters

To determine the rise in temperature, we identify the following constants and variables provided by the problem statement:

  • Power of the drilling machine ($P$) = $10\text{ kW} = 10 \times 10^3\text{ W} = 10,000\text{ J/s}$
  • Mass of the aluminium block ($m$) = $8.0\text{ kg} = 8,000\text{ g}$
  • Time duration ($t$) = $2.5\text{ minutes} = 2.5 \times 60\text{ s} = 150\text{ s}$
  • Specific heat of aluminium ($c$) = $0.91\text{ J g}^{-1}\text{ K}^{-1} = 910\text{ J kg}^{-1}\text{ K}^{-1}$
  • Efficiency ($\eta$) = $50\% = 0.5$

Step 2: Calculating Effective Heat Energy Absorbed

The total work done by the machine is given by $W = P \times t$. Since only $50\%$ of the power is used to heat the aluminium block, the heat energy ($Q$) absorbed by the block is:

$Q = \eta \times P \times t$

$Q = 0.5 \times 10,000\text{ J/s} \times 150\text{ s}$

$Q = 5,000 \times 150 = 750,000\text{ J}$

[Per the definition of energy transfer where $Q = \text{Power} \times \text{Time} \times \text{Efficiency}$]

Step 3: Calculating Rise in Temperature

Using the principle of calorimetry, the heat absorbed is related to the change in temperature ($\Delta T$) by the formula:

$Q = mc\Delta T$

Rearranging the formula to solve for $\Delta T$:

$\Delta T = \frac{Q}{mc}$

Substituting the known values:

$\Delta T = \frac{750,000\text{ J}}{(8.0\text{ kg}) \times (910\text{ J kg}^{-1}\text{ K}^{-1})}$

$\Delta T = \frac{750,000}{7,280}$

$\Delta T \approx 103.02\text{ K}$

Visual Representation of Energy Flux

Drill Output Al Block m=8kg 50% Effective

Analytical Summary

Parameter Value
Total Energy Supplied $1.5 \times 10^6\text{ J}$
Heat Absorbed ($Q$) $7.5 \times 10^5\text{ J}$
Temperature Rise ($\Delta T$) $103.02\text{ K}$

Final Solution: The rise in temperature of the aluminium block is approximately 103.02 K.

Solution:

Step 1: Analyzing the Fundamental Basis of Gas Thermometry

The temperature $T$ recorded by a constant-volume gas thermometer is defined by the relation:

$T = 273.16 \left( \frac{p}{p_{tr}} \right)$

where $p$ is the pressure of the gas at temperature $T$, and $p_{tr}$ is the pressure at the triple point of water ($273.16 \, K$). This definition assumes that the gas behaves as an ideal gas [Per the Ideal Gas Law $PV = nRT$].

Step 2: Identifying the Source of Discrepancy

The "slight difference" arises because real gases, such as Oxygen ($O_2$) and Hydrogen ($H_2$), deviate from ideal gas behavior under experimental conditions. Specifically:

  • Intermolecular Forces: Real gases possess finite intermolecular attractions and repulsions, which are not accounted for in the ideal gas model.
  • Molecular Volume: Real gas molecules occupy a finite volume, unlike point-mass particles in an ideal gas.
  • Gas Specificity: The magnitude of deviation from ideality depends on the nature of the gas (its molar mass, boiling point, and van der Waals constants $a$ and $b$). Since $O_2$ and $H_2$ have different molecular properties, they exhibit different pressure-temperature curves at non-zero pressures.

Step 3: Defining the Procedure for Discrepancy Reduction

To align the readings, one must approach the limit where real gases behave as ideal gases. This is achieved by systematically reducing the gas density.

The Procedure:

  1. Measure the temperature $T$ at various lower initial pressures ($p_{tr,1}, p_{tr,2}, \dots, p_{tr,n}$) at the triple point.
  2. Plot the values of $T$ obtained for each pressure against the pressure $p_{tr}$.
  3. Extrapolate the graph to the intercept where $p_{tr} \rightarrow 0$.
  4. At the limit $p_{tr} \rightarrow 0$, the gas behaves as an ideal gas, and the readings of both thermometers will converge to the same value.
Pressure at Triple Point (p_tr) Temperature (T) Oxygen Hydrogen Converged T

Step 4: Theoretical Justification

This approach relies on the van der Waals Equation of State:

$\left( P + \frac{an^2}{V^2} \right) (V - nb) = nRT$

As $p \rightarrow 0$, the volume $V \rightarrow \infty$, making the correction terms $\frac{an^2}{V^2}$ and $nb$ negligible. Consequently, the equation simplifies to $PV \approx nRT$, rendering the gas perfectly ideal and eliminating the instrument-dependent discrepancy [Per Kinetic Theory of Gases].

Final Solution: The discrepancy is caused by the deviation of real gases ($O_2$ and $H_2$) from ideal behavior. The discrepancy can be reduced by taking measurements at successively lower pressures and extrapolating the result to zero pressure ($p_{tr} \rightarrow 0$).

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