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How does transient heat transfer differ from steady heat transfer? How does one-dimensional heat transfer differ from two-dimensional heat transfer?

Short Answer

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Answer: The main differences between transient and steady heat transfer are related to the constancy of the temperature distribution within the system: transient heat transfer involves temperature distribution changes over time, while steady heat transfer maintains constant temperature distribution. The primary differences between one-dimensional and two-dimensional heat transfers involve spatial considerations: one-dimensional heat transfer assumes heat transfer occurs in one direction, while two-dimensional heat transfer accounts for variations in temperature and heat flow in two spatial directions.

Step by step solution

01

Definition of Transient Heat Transfer

Transient heat transfer refers to the process where the temperature distribution within a system changes over time. This occurs when the heat transfer rate within the system is time dependent, which means that the rate at which heat is transferred is not constant.
02

Definition of Steady Heat Transfer

Steady heat transfer, on the other hand, is the process where the temperature distribution within a system remains constant over time. In this case, the heat transfer rate is time independent, meaning that the rate at which heat is being transferred remains constant.
03

Differences between Transient and Steady Heat Transfer

The main difference between transient and steady heat transfer is the constancy of the temperature distribution within the system. In transient heat transfer, the temperature distribution changes over time, whereas in steady heat transfer, the temperature distribution remains constant. In other words, a system experiencing transient heat transfer will eventually reach a steady state, where the temperature distribution stops changing, and steady heat transfer takes place.
04

Definition of One-dimensional Heat Transfer

One-dimensional heat transfer is a simplification of the heat transfer process in which heat transfer is assumed to take place only in one direction within the system. This type of heat transfer is usually applied to cases with large differences in conductivity or thickness in one direction compared to others, such as a long rod or a wall.
05

Definition of Two-dimensional Heat Transfer

Two-dimensional heat transfer accounts for heat transfer in two spatial directions within a system. This is a more realistic representation of the heat transfer process and is typically used when the temperature distribution varies in two directions. Examples of two-dimensional heat transfer include heat transfer in a rectangular plate or across the corner of a wall.
06

Differences between One-dimensional and Two-dimensional Heat Transfer

The primary difference between one-dimensional and two-dimensional heat transfer lies in the spatial considerations. One-dimensional heat transfer is a simplification that assumes heat transfer occurs only in one direction, while two-dimensional heat transfer accounts for variations in temperature and heat flow in two spatial directions. Understanding the correct dimensionality of a given problem is essential for accurate analysis and modeling of the heat transfer process.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Transient Heat Transfer
Transient heat transfer occurs when temperature changes over time. This means the heat transfer rate varies as the system evolves.
Think of it like a boiling pot of water, where the temperature heats up until it reaches boiling point. During transient heat transfer, the system is not in equilibrium. Everything is in motion—energy is being exchanged.
Factors that influence transient heat transfer include:
  • Material properties: Different materials conduct heat at different rates.
  • Initial conditions: The starting temperature distribution of the system.
  • Boundary conditions: How heat enters or leaves the system.
Understanding transient heat transfer is crucial for designing systems that need to reach desired temperatures over time.
Steady Heat Transfer
Steady heat transfer is characterized by a constant temperature distribution over time. Once equilibrium is achieved, the temperature stops changing.
This is like steady sunshine warming a brick wall to a certain temperature, which then remains stable. The system is in balance—the rate of heat entering is the same as the rate of heat leaving.
Key aspects of steady heat transfer include:
  • Constant thermal conditions: No change in temperature as time progresses.
  • Fixed heat transfer rate: Energy flows consistently over time.
This concept is widely used in engineering, as it simplifies calculations and designs for thermal systems in equilibrium.
One-dimensional Heat Transfer
In one-dimensional heat transfer, heat moves in just one direction. Solutions to these problems assume minimal variation across other dimensions.
Picture a long, heated metal rod. Heat travels along its length, but not much elsewhere. This simplification is useful when differences in geometry or material properties are significant along one axis.
Essential points of one-dimensional heat transfer:
  • Suitable for slender configurations: Long rods, thin slabs.
  • Assumes negligible lateral heat conduction.
This approach is often the first step in analyzing complex heat transfer scenarios by reducing the problem to its simplest form.
Two-dimensional Heat Transfer
Two-dimensional heat transfer accounts for heat flow in two perpendicular directions. This offers a more realistic depiction of how heat moves through surfaces, like in a flat plate.
Imagine heat spreading across a wall corner. It doesn’t just flow straight down; it also spreads sideways. This type of analysis is vital for structures with significant temperature gradients in two dimensions.
Important considerations for two-dimensional heat transfer include:
  • Complex geometry: Often applied to plates, walls, or regions with uneven heat application.
  • More intricate calculations: Requires more advanced mathematical methods.
Understanding this concept helps engineers design more efficient cooling and heating systems across various fields.
Temperature Distribution
Temperature distribution refers to how temperature varies within a material or system. It can be a simple gradient or a complex pattern depending on conditions and materials.
Imagine a pie cooling down on a window sill. The temperature is higher in the center and cooler at the edges, forming a gradient.
Factors influencing temperature distribution:
  • Material properties: Conductivity, density, and specific heat.
  • Heat source and sink locations: Where heat is added or removed.
  • System geometry: Shape and size affect distribution patterns.
Understanding temperature distribution is key for predicting system behavior and optimizing designs for efficiency and safety.

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Most popular questions from this chapter

How is integration related to derivation?

A spherical vessel is filled with chemicals undergoing an exothermic reaction. The reaction provides a uniform heat flux on the inner surface of the vessel. The inner diameter of the vessel is \(5 \mathrm{~m}\) and its inner surface temperature is at \(120^{\circ} \mathrm{C}\). The wall of the vessel has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where \(k_{0}=1.01 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), \(\beta=0.0018 \mathrm{~K}^{-1}\), and \(T\) is in \(\mathrm{K}\). The vessel is situated in a surrounding with an ambient temperature of \(15^{\circ} \mathrm{C}\), the vessel's outer surface experiences convection heat transfer with a coefficient of \(80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). To prevent thermal burn on skin tissues, the outer surface temperature of the vessel should be kept below \(50^{\circ} \mathrm{C}\). Determine the minimum wall thickness of the vessel so that the outer surface temperature is \(50^{\circ} \mathrm{C}\) or lower.

Consider a large 5-cm-thick brass plate \((k=\) \(111 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) ) in which heat is generated uniformly at a rate of \(2 \times 10^{5} \mathrm{~W} / \mathrm{m}^{3}\). One side of the plate is insulated while the other side is exposed to an environment at \(25^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(44 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Explain where in the plate the highest and the lowest temperatures will occur, and determine their values.

Exhaust gases from a manufacturing plant are being discharged through a 10 - \(\mathrm{m}\) tall exhaust stack with outer diameter of \(1 \mathrm{~m}\), wall thickness of \(10 \mathrm{~cm}\), and thermal conductivity of \(40 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The exhaust gases are discharged at a rate of \(1.2 \mathrm{~kg} / \mathrm{s}\), while temperature drop between inlet and exit of the exhaust stack is \(30^{\circ} \mathrm{C}\), and the constant pressure specific heat of the exhaust gasses is \(1600 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\). On a particular day, the outer surface of the exhaust stack experiences radiation with the surrounding at \(27^{\circ} \mathrm{C}\), and convection with the ambient air at \(27^{\circ} \mathrm{C}\) also, with an average convection heat transfer coefficient of \(8 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Solar radiation is incident on the exhaust stack outer surface at a rate of \(150 \mathrm{~W} / \mathrm{m}^{2}\), and both the emissivity and solar absorptivity of the outer surface are 0.9. Assuming steady one-dimensional heat transfer, (a) obtain the variation of temperature in the exhaust stack wall and (b) determine the inner surface temperature of the exhaust stack.

A cylindrical nuclear fuel rod of \(1 \mathrm{~cm}\) in diameter is encased in a concentric tube of \(2 \mathrm{~cm}\) in diameter, where cooling water flows through the annular region between the fuel rod \((k=30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) and the concentric tube. Heat is generated uniformly in the rod at a rate of \(50 \mathrm{MW} / \mathrm{m}^{3}\). The convection heat transfer coefficient for the concentric tube surface is \(2000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the surface temperature of the concentric tube is \(40^{\circ} \mathrm{C}\), determine the average temperature of the cooling water. Can one use the given information to determine the surface temperature of the fuel rod? Explain.

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