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Layers of 6-in-thick meat slabs $(k=0.26 \mathrm{Btu} /$ $\mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}$ and $\alpha=1.4 \times 10^{-6} \mathrm{ft}^2 / \mathrm{s}$ ) initially at a uniform temperature of $50^{\circ} \mathrm{F}$ are cooled by refrigerated air at $23^{\circ} \mathrm{F}$ to a temperature of $36^{\circ} \mathrm{F}$ at their center in 12 h . Estimate the average heat transfer coefficient during this cooling process.

   Layers of 6-in-thick meat slabs $(k=0.26 \mathrm{Btu} /$ $\mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}$ and $\alpha=1.4 \times 10^{-6} \mathrm{ft}^2 / \mathrm{s}$ ) initially at a uniform temperature of $50^{\circ} \mathrm{F}$ are cooled by refrigerated air at $23^{\circ} \mathrm{F}$ to a temperature of $36^{\circ} \mathrm{F}$ at their center in 12 h . Estimate the average heat transfer coefficient during this cooling process.
 
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Introduction To Thermodynamics and Heat Transfer
Introduction To Thermodynamics and Heat Transfer
Yunus A. Cengel 1st Edition
Chapter 11, Problem 61 ↓

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5 ft - Thermal conductivity k = 0.26 Btu/h·ft·°F - Thermal diffusivity α = 1.4 × 10^-6 ft²/s - Initial temperature Ti = 50°F - Ambient temperature T∞ = 23°F - Final center temperature = 36°F - Cooling time t = 12 h  Show more…

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Layers of 6-in-thick meat slabs $(k=0.26 \mathrm{Btu} /$ $\mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}$ and $\alpha=1.4 \times 10^{-6} \mathrm{ft}^2 / \mathrm{s}$ ) initially at a uniform temperature of $50^{\circ} \mathrm{F}$ are cooled by refrigerated air at $23^{\circ} \mathrm{F}$ to a temperature of $36^{\circ} \mathrm{F}$ at their center in 12 h . Estimate the average heat transfer coefficient during this cooling process.
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Key Concepts

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Heat Transfer Coefficient
This is a parameter that quantifies the convective heat transfer between a surface and its surrounding fluid. It relates the rate of heat transfer per unit area to the temperature difference between the surface and the fluid. In engineering applications, accurately estimating the heat transfer coefficient is crucial for designing efficient cooling or heating systems, as it governs how fast a body can reach thermal equilibrium with its environment.
Transient Conduction in Solids
Transient conduction refers to the time?dependent process of heat transfer through a solid body. Instead of assuming a steady state, the temperature field within the body changes with time as it responds to thermal boundary conditions. Analyzing transient conduction is essential for processes where the system’s temperature evolves over time, such as the cooling of a hot object, and typically involves solving the heat diffusion equation subject to initial and boundary conditions.
Newton’s Law of Cooling
Newton’s Law of Cooling provides a boundary condition that links the convective heat flux at a solid surface to the temperature difference between the surface and the surrounding fluid. This law expresses the heat loss (or gain) per unit area as proportional to the difference in temperature, with the proportionality constant being the heat transfer coefficient. It is widely used to model situations where a solid is exposed to a fluid environment.
Dimensionless Numbers (Biot and Fourier Numbers)
Dimensionless numbers such as the Biot and Fourier numbers play a crucial role in transient heat transfer analysis. The Biot number compares the internal conduction resistance to the external convective resistance, indicating whether the lumped capacitance method is appropriate. The Fourier number represents the ratio of heat conduction rate to the rate of thermal energy storage in a material. These numbers help in scaling the problem and simplifying the analysis of temperature distributions in heated or cooled bodies.

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