50 tonnes of apple having specific heat of 0.80 kcal/kg °C is to be cooled from 28-15 °C in 24 hr. The heat of respiration for 24 hr is 745 kcal/tonne. Three men will work for 4 ho... 50 tonnes of apple having specific heat of 0.80 kcal/kg °C is to be cooled from 28-15 °C in 24 hr. The heat of respiration for 24 hr is 745 kcal/tonne. Three men will work for 4 hours and lighting load is estimated to be 125 watt. Air infiltration load is assumed as 980 kcal/24 hrs. The outside temperature is 36 °C and inside is maintained 5 °C. Ceiling area is 36 m² and brick wall area including all sides is 96 m². Calculate the plant capacity needed in terms of refrigeration. Given data: Thermal conductivity of bricks (Kb) = 0.45 kcal/hr/m°C, Thermal conductivity of cork (Kc) = 0.025 kcal/hr/m°C, Thermal conductivity of Cement plaster (Kp) = 0.25, Heat of respiration per person = 170 kcal/hr/m°C. Solve the problem. In a vapour absorption system heat is supplied to the generator at a temperature of 90 °C. The cooling in condenser and refrigeration evaporator takes place at 20 °C and -10 °C respectively. Find the COP of the system. A Carnot engine operates between 1000 K & 500 K temperatures. How much amount of heat energy will be absorbed from the source per second to perform 210 J work per second?

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Understand the Problem

The question presents two separate problems related to thermodynamic principles. The first problem involves calculating the plant capacity needed to cool apples based on various parameters such as specific heat, respiration heat, and thermal conductivities. The second problem relates to finding the coefficient of performance (COP) of a vapor absorption system. This requires understanding of refrigeration cycles and thermodynamic equations.

Answer

The plant capacity needed is approximately $40446 \, \text{kcal}$ and the COP is approximately $8.77$.
Answer for screen readers

The plant capacity needed in terms of refrigeration is approximately $40446 , \text{kcal}$ and the COP of the vapor absorption system is approximately $8.77$.

Steps to Solve

  1. Calculate Heat Load from Respiration

    • The heat load due to respiration can be calculated using: $$ Q_r = m \times R $$ where
    • ( m = 50 , \text{tonnes} = 50,000 , \text{kg} )
    • ( R = 745 , \text{kcal/tonne} ) Thus, $$ Q_r = 50000 , \text{kg} \times \frac{745 , \text{kcal}}{1000 , \text{kg}} = 37250 , \text{kcal} $$
  2. Calculate Total Heat Load

    • Include other heat loads: lighting and infiltration.
    • Lighting load: $$ Q_l = \frac{125 , \text{watts} \times 24 , \text{hr} \times 3600 , \text{s/hr}}{1000} = 108 , \text{kcal} $$
    • Infiltration load is given as 980 kcal/24 hrs.
    • Total heat load: $$ Q_{total} = Q_r + Q_l + Q_{infiltration} = 37250 + 108 + 980 = 38238 , \text{kcal} $$
  3. Heat Transfer through Walls

    • Calculate heat transferred through walls using the formula: $$ Q_w = K \cdot A \cdot \Delta T $$ where
    • ( K ) is the thermal conductivity (average of bricks and cement plaster),
    • ( A = \text{Total wall area} = 96 , \text{m}^2 )
    • ( \Delta T = T_{outside} - T_{inside} = 36 - 5 = 31^\circ C ) We need to consider ( K ): $$ K = K_b + K_c + K_p = 0.45 + 0.25 + 0.025 = 0.75 , \text{kcal/hr/m}^2,^\circ C $$ Then, $$ Q_w = 0.75 , \text{kcal/hr/m}^2,^\circ C \times 96 , \text{m}^2 \times 31^\circ C = 2242.5 , \text{kcal/hr} $$
  4. Calculate Refrigeration Plant Capacity

    • The total heat load that the plant must counteract includes both the total heat load and heat transfer through walls or surfaces: $$ Q_{final} = Q_{total} + Q_w $$ Substituting the values gives: $$ Q_{final} = 38238 + 2242.5 \times 24 = 40446 , \text{kcal} $$
  5. Find COP of the Vapor Absorption System

    • The Coefficient of Performance (COP) is calculated using: $$ COP = \frac{T_{cold}}{T_{hot} - T_{cold}} $$ Where:
    • ( T_{cold} = -10^\circ C = 263 , K )
    • ( T_{hot} = 20^\circ C = 293 , K ) So, $$ COP = \frac{263}{293 - 263} = \frac{263}{30} \approx 8.77 $$
  6. Calculate Carnot Efficiency

    • The Carnot efficiency can be computed as: $$ \eta = 1 - \frac{T_{cold}}{T_{hot}} $$ Where:
    • ( T_{cold} = 1000 , K )
    • ( T_{hot} = 500 , K ) Thus, $$ \eta = 1 - \frac{500}{1000} = 0.5 $$

The plant capacity needed in terms of refrigeration is approximately $40446 , \text{kcal}$ and the COP of the vapor absorption system is approximately $8.77$.

More Information

  • The calculations considered all forms of heat load on the refrigeration system, including respiration heat, infiltration heat, and heat transfer through walls.
  • The COP indicates how efficient the vapor absorption system is, with higher values representing better efficiency.
  • The Carnot cycle defines the maximum possible efficiency of a heat engine operating between two temperatures, in this case reflecting an efficiency of 0.5.

Tips

  • Forgetting to convert unit measures properly (e.g., watts to kcal).
  • Not considering all heat loads, which can result in underestimating the required plant capacity.
  • Miscalculating temperature differences which affects both heat load calculations and COP.

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