Heat transfer is a fundamental process in both nature and technology, driving everything from weather patterns to the performance of your home’s heating system. At its core, heat transfer occurs due to temperature differences, moving thermal energy from warmer regions to cooler ones. Let's dive into the three primary modes of heat transfer: conduction, convection, and radiation.
Conduction: Heat Through Direct Contact
Conduction is the process of heat transfer through direct molecular collision. When particles in a material—whether it's a solid, liquid, or gas—come into contact with each other, they transfer energy from the hotter particles to the cooler ones.
How It Works: In solids, conduction occurs as vibrating particles transfer energy to neighboring particles. In liquids and gases, while conduction is less efficient due to the greater distance between particles, it still happens through molecular interactions.
Example: Think of a metal spoon in a hot cup of coffee. The heat from the coffee is conducted through the spoon, eventually warming the handle that you might touch.
Convection: Heat Through Fluid Movement
Convection is the primary mode of heat transfer in fluids (liquids and gases). Unlike conduction, which relies on direct particle interaction, convection involves the bulk movement of fluid.
How It Works: In convection, warmer, less dense fluid rises while cooler, denser fluid sinks. This movement creates a convection current, which circulates heat throughout the fluid.
Types of Convection:
Forced Convection: This occurs when an external force, like a fan or pump, moves the fluid. For example, an air conditioner uses a fan to blow air over a condenser coil, improving heat transfer efficiency.
Natural Convection: This type of convection happens without external aid. For instance, in a warehouse, warm air rises and escapes from vents, while cooler air moves in to replace it, creating a natural circulation pattern.
Radiation: Heat Through Electromagnetic Waves
Radiation differs from conduction and convection in that it doesn’t require a medium. Instead, heat is transferred via electromagnetic waves, which can travel through a vacuum.
How It Works: Electromagnetic waves, such as light and infrared radiation, are produced by the vibration of electric charges. These waves can travel through empty space at the speed of light (approximately 3 x 10^8 meters per second).
Key Concepts:
Emissivity: When radiant energy hits a surface, some is reflected, some is transmitted, and the rest is absorbed. The fraction absorbed is known as emissivity. A perfect black body has an emissivity of 1, meaning it absorbs all incident radiation, while a perfect white body has an emissivity of 0, reflecting all radiation.
Stefan-Boltzmann Law: This law states that the total radiant heat energy emitted by a surface is proportional to the fourth power of its absolute temperature (T). The formula is:
where is the radiant heat energy emitted per unit area per second, is the absolute temperature in Kelvin, and (the Stefan-Boltzmann constant) is .
Radiant Energy Exchange: When a body at temperature is surrounded by an environment at temperature , the net radiant energy exchange can be described by:
where is the surface area in square meters, and γ is the emissivity. If is greater than , the body emits more energy than it absorbs, cooling down. Conversely, if is less than , the body absorbs more energy than it emits, heating up.
Understanding these modes of heat transfer helps us design better systems for heating, cooling, and energy efficiency in a variety of applications. Whether it’s the metal spoon in your coffee, the warm air rising in your home, or the sunlight warming your skin, these principles of heat transfer are at work all around us. By grasping how conduction, convection, and radiation operate, we can better appreciate the dynamics of thermal energy in our everyday lives.
Fourier’s Law of Heat Conduction: Understanding the Relation Between Heat Flux and Temperature Gradient
When dealing with heat transfer through materials, particularly in the context of conduction, Fourier’s Law plays a crucial role. This law provides a foundational understanding of how heat moves through a substance and helps solve various engineering and scientific problems related to thermal energy. Here’s a deeper dive into Fourier’s Law of Conduction and how it applies to heat transfer through materials.
Fourier’s Law of Conduction: The Basics
Fourier’s Law of Conduction states that the rate of heat transfer (heat flux) through a material is directly proportional to the temperature gradient in the direction of heat flow. In simpler terms, heat moves from regions of higher temperature to regions of lower temperature, and the rate at which this heat transfer occurs is influenced by how steep the temperature gradient is.
Mathematical Formulation:
At any given location, the heat transfer rate per unit area (heat flux) in a specific direction is given by:
where:
- is the heat flux (W/m²),
- is the thermal conductivity of the material (W/m·K),
- is the temperature gradient in the x-direction,
- The negative sign indicates that heat flows in the direction of decreasing temperature.
Calculating Heat Transfer Rate Across a Surface
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Linear Temperature Profile in a Rectangular Slab
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To determine the actual heat transfer rate through a material, Fourier’s Law can be expressed as:
where:
- is the heat transfer rate (W or J/s),
- is the thermal conductivity of the material (W/m·K),
- is the surface area normal to the heat flow direction (m²),
- and are the temperatures on either side of the material (K or °C),
- is the thickness of the material through which heat is being transferred (m).
Note: is positive if is greater than , indicating that heat flows from the higher temperature side to the lower temperature side.
Heat Conduction Through a Plane Wall
In many practical scenarios, heat conduction through a plane wall is a common problem. The heat transfer rate through a plane wall can be described by:
where the thermal resistance is defined as:
Here’s what each symbol represents:
- = Thickness of the wall (m),
- = Thermal conductivity of the material (W/m·K),
- = Surface area of the wall normal to the direction of heat flow (m²),
- = Temperature on the outside wall surface (K or °C),
- = Temperature on the inside wall surface (K or °C),
- = Heat transfer rate (W or J/s).
Assumptions for Fourier’s Law
For Fourier’s Law to be applicable and for the above equations to hold true, several assumptions are typically made:
- Steady-State Conditions: The temperature distribution within the material does not change with time.
- Homogeneous Material: The material has uniform properties throughout.
- Constant Thermal Conductivity: The thermal conductivity k is constant and does not vary with temperature.
- One-Dimensional Heat Flow: Heat transfer is considered to occur in one direction only, simplifying the analysis to a single spatial dimension.
- Uniform Surface Temperatures: The temperatures on the surfaces of the material are uniform.
SAMPLE PROBLEM:
The outer wall of a house, constructed with common brick, is 4-m long , 2-m high, and 30-cm thick. The inner surface of the wall is at 20 °C and the outer surface at O °C (cold days). Find the heat transfer rate through the wall.
Heat Flow Through a Plane Wall
When dealing with heat transfer through a plane wall exposed to convective heat transfer on both sides, it’s essential to consider both conduction through the wall and convection to and from the wall’s surfaces. This combined analysis allows us to understand how thermal energy moves through the wall and interacts with the surrounding air.
Heat Transfer Equation with Convective Boundaries
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Determining Conductive Heat Transfer Rate with Boundaries Exposed to Convective Heat Transfer (a) Model of wall (b) Temp. distribution in the wall & the Fluids |
For a plane wall exposed to convective heat transfer on both sides, the heat transfer rate q can be determined using the following equation:
where:
- = Inside air temperature (K or °C)
- = Outside air temperature (K or °C)
- = Convective heat transfer coefficient for the inside air (W/m²·K)
- = Convective heat transfer coefficient for the outside air (W/m²·K)
- = Thermal conductivity of the wall material (W/m·K)
- = Thickness of the wall (m)
- = Surface area of the wall (m²)
Explanation of Terms and Calculation
Convective Heat Transfer Coefficients
The convective heat transfer coefficients and vary depending on the nature of the fluid flow and its speed:
- Low-Speed Air Flow: Typical value around 10 W/m²·K.
- Moderate-Speed Air Flow: Typical value around 100 W/m²·K.
These values reflect how efficiently heat is transferred between the wall surface and the surrounding air.
Heat Transfer Rate
To calculate the heat transfer rate through the wall, we use the thermal resistances due to convection and conduction. The total resistance is the sum of the resistances due to convection on both sides of the wall and conduction through the wall:
- Convective Resistance (Inside):
- Conductive Resistance (Through Wall):
- Convective Resistance (Outside):
The heat transfer rate is then calculated by taking the temperature difference between the inside and outside air and dividing it by the total thermal resistance:
Electrical Analogy and Energy Balance
The heat transfer equation can also be derived using an energy balance approach, which is analogous to an electrical circuit:
Energy Balance on the Left Surface of the Wall:
- Heat transfer rate by convection from the fluid at to the surface () is equal to the heat transfer rate by conduction within the wall ().
Energy Balance on the Right Surface of the Wall:
- Heat transfer rate by conduction within the wall () is equal to the heat transfer rate by convection from the surface to the fluid at ().
In steady-state conditions, the heat transfer rate across every cross-section of the wall is constant. Thus:
The equations for heat transfer rates are:
-
Rearranging these equations and summing the temperature differences, we get:
Adding these equations yields:
Solving for q, we obtain the final equation:
SAMPLE PROBLEM: |
The resistances are in series, so the heat transfer rate through all the resistances is the same, however, there is a temperature drop per resistance.
Heat Flow Through a Composite Wall with Convection BoundariesWhen dealing with walls made of multiple materials, such as in building construction, the heat transfer process becomes more complex due to the different thermal properties of each material. Additionally, convective heat transfer on the surfaces further complicates the analysis. Here's how to approach this problem using the concept of thermal resistance and overall heat transfer coefficients. Understanding Thermal Resistance in a Composite WallFor a composite wall consisting of several layers of different materials, the thermal resistances are arranged in series. Each layer of material and each convective boundary contribute to the overall thermal resistance of the wall. Thermal Resistance CalculationThe overall thermal resistance R of a composite wall with convective boundaries is the sum of the resistances of each layer plus the resistances due to convection on both sides. Mathematically, this is expressed as: where: - = Convective resistance on the outside surface
- = Conductive resistance through material A
- = Conductive resistance through material B
- = Conductive resistance through material C
- = Convective resistance on the inside surface
- , , and = Thicknesses of materials A, B, and C respectively
- , , = Thermal conductivities of materials A, B, and C respectively
- and = Convective heat transfer coefficients for inside and outside surfaces
The overall heat flow rate through the composite wall is then given by: where: - = Inside air temperature
- = Outside air temperature
- = Overall thermal resistance of the wall
Typical Convective Heat Transfer CoefficientsFor practical purposes, the convective heat transfer coefficients are often approximated based on average conditions: - Inside Surfaces: For zero air speed, approximately .
- Outside Surfaces: For a wind speed of 15 mph, approximately .
Heat Transfer Through a Composite Wall with Series ResistancesWhen analyzing heat flow through a composite wall comprising multiple materials, it's essential to understand how resistances to heat transfer are combined and how to calculate the overall heat transfer rate. In this context, resistances are considered to be in series, and the overall heat transfer coefficient helps simplify the calculations. Here's a detailed look at how these concepts work. Resistance in SeriesIn a composite wall with multiple layers and convective boundaries, the thermal resistances of each layer and the convective resistances on the surfaces are arranged in series. This configuration implies that heat must pass through each resistance sequentially. Heat Transfer Rate and Temperature DropsWhen resistances are in series, the same heat transfer rate Q flows through each resistance. The relationship can be expressed as: where: - are the temperatures at different points across the resistances.
- are the individual thermal resistances.
- is the overall temperature difference across the wall.
The individual temperature drops across each resistance are:
By summing these temperature drops, we get:
Thus, the overall heat transfer rate can be expressed as: where is the total thermal resistance of the composite wall. Overall Heat Transfer Coefficient (U-Value)To simplify the calculation of heat transfer through a composite wall with multiple resistances, the overall heat transfer coefficient is used. The -value represents how well heat is transferred through the wall and is defined as:
where: - is the overall heat transfer coefficient (W/m²·K),
- is the surface area of the wall (m²),
- is the temperature difference across the wall (K or °C),
- is the heat flow rate (W).
By rearranging this equation, the relationship between and the overall thermal resistance is given by:
or equivalently: Applying the Overall Heat Transfer CoefficientFor a composite wall with several layers and convective boundaries, the overall heat transfer coefficient is computed by summing the individual resistances: where: - and represent the convective resistances on the inside and outside surfaces, respectively,
- , , and are the conductive resistances through the different materials.
The overall heat transfer coefficient is then the reciprocal of this sum: When analyzing heat flow through a composite wall with series resistances, it is crucial to combine the resistances from each layer and the convective boundaries. The overall thermal resistance can be computed by summing individual resistances, and the overall heat transfer coefficient U simplifies the calculation of heat flow through the wall. By understanding these concepts, you can effectively evaluate and design walls for optimal thermal performance and energy efficiency. SAMPLE PROBLEM: The exterior wall of a building is constructed of four materials:12-mm thick gypsum board, 75-mm thick fiberglass insulation , 20-mm thick plywood, and 20-mm thick hardboard siding. The inside and outside air temperatures are 20 °C and -10 °C, respectively. The convective heat transfer coefficient on the inner and outer surfaces of the wall are 6 W/m² °C and 10 W/m² °C, respectively. Determine the rate of heat transfer and the overall heat transfer coefficient. | The thermal Circuit of a One-Dimensional Temperature Distribution Problem (a) A composite wall exposed to fluids on either side at different temperatures and the corresponding circuit. (b) Temp profile in the composite wall.
Heat Conduction Through a Hollow CylinderHeat conduction through a hollow cylinder or pipe involves analyzing the thermal resistance in the radial direction. This problem is common in applications like pipes, ducts, and insulated cylinders. Understanding the heat transfer through such geometries requires calculating the thermal resistance and heat flow, taking into account both conductive and convective resistances. Heat Conduction through a Hollow Cylinder-The inner and outer Temperatures are Maintained at Uniform Temperatures Ti and To. Basic Heat Conduction in a Hollow CylinderFor a hollow cylinder or pipe, the heat transfer rate due to conduction is given by: where: - = Inside wall temperature
- = Outside wall temperature
- = Overall thermal resistance of the cylinder
The thermal resistance for a cylindrical shell can be calculated using: where: - = Inside radius of the cylinder
- = Outside radius of the cylinder
- = Length of the cylinder
- = Thermal conductivity of the material
In terms of heat flow , this becomes:
Heat Conduction with Convection BoundariesWhen convection is present on both the inner and outer surfaces of the cylinder, the total thermal resistance includes both convective and conductive components: where: - = Convective heat transfer coefficient on the inside surface
- = Convective heat transfer coefficient on the outside surface
- = Inside surface area
- = Outside surface area
The heat flow rate q is then: where: - = Fluid temperature inside the cylinder
- = Surrounding temperature outside the cylinder
Example CalculationFor a tube with convection boundaries: Thus, the heat flow rate is: Heat Flow Through an Insulated PipeIf a pipe is covered with insulation and the convection boundaries are neglected, the heat flow rate q through the pipe with insulation is calculated as: where: - = Thermal conductivity of the pipe material
- = Thermal conductivity of the insulation
- = Inner radius of the pipe
- = Outer radius of the pipe
- = Outer radius of the insulation
- = Length of the pipe
Heat Flow Through a Composite Cylinder with Multiple Layers
For a composite cylinder with multiple layers and convection boundaries, the overall thermal resistance is the sum of resistances from each layer and the convective resistances: where: - , , are the thermal conductivities of the respective layers.
- , , , are the radii of the different layers.
The heat flow rate can be calculated as:
Analyzing heat conduction through a hollow cylinder involves calculating thermal resistances due to conduction and convection. For a composite cylinder, the overall thermal resistance includes resistances from each layer and convective boundaries. By understanding these concepts, you can accurately determine heat transfer rates and design systems for effective thermal management. SAMPLE PROBLEM: Consider a person standing in a breezy room at 20°C. Determine the total rate heat transfer from this person if the exposed surface area and the average outer surface temperature of the person are 1.62 m and 29 °C , respectively, and the convection heat transfer coefficient is 6W/m² °C .
Forced Convection: Understanding Heat Transfer with External Fluid MotionForced convection is a crucial concept in heat transfer, especially in systems where fluid motion is induced by external means such as fans or pumps. Unlike natural convection, where fluid motion is driven by buoyancy effects due to temperature differences, forced convection relies on mechanical means to move the fluid. This blog delves into the principles of forced convection, its important parameters, and its application in practical scenarios like heat exchangers and tube banks. Key Parameters in Forced ConvectionIn forced convection, several parameters are used to characterize the heat transfer process: Nusselt Number (Nu): The Nusselt number quantifies the ratio of convective to conductive heat transfer and is used to determine the convective heat transfer coefficient . Here, is the characteristic length and is the thermal conductivity of the fluid. Reynolds Number (Re): Re=μρVLThe Reynolds number measures the ratio of inertial forces to viscous forces within the fluid. It is a dimensionless quantity where is the fluid density, is the fluid velocity, is the characteristic length, and is the dynamic viscosity of the fluid. Prandtl Number (Pr): The Prandtl number relates the fluid's momentum diffusivity (viscosity) to its thermal diffusivity. Here, is the specific heat capacity of the fluid at constant pressure. Convective Heat Transfer Coefficient (h):
This coefficient indicates how effectively heat is transferred from a surface to the fluid. Characteristic Length (L):
The length used to describe the geometry of the heat transfer surface. Thermal Conductivity (k):
The property of the fluid that indicates how well it conducts heat. Density (ρ):
The mass per unit volume of the fluid. Velocity (V):
The speed at which the fluid flows. Dynamic Viscosity (μ):
The measure of a fluid's internal resistance to flow. Kinematic Viscosity (ν):
The ratio of dynamic viscosity to density, . Thermal Diffusivity (α):
The ratio of thermal conductivity to the product of density and specific heat capacity, .
Forced Convection in Tube BanksIn many practical applications, such as heat exchangers, forced convection occurs when a fluid flows over a bank of tubes. The configuration and arrangement of these tubes significantly impact the heat transfer characteristics. Velocity Between Tubes:
The maximum velocity of the fluid between two tubes can be expressed as: where is the free stream velocity, is the spacing between tubes, and is the diameter of the tubes. If , the maximum velocity approaches the free stream velocity, and the flow resembles that over a single cylinder. Otherwise, significant velocity increases occur between the tubes in each row. Effect of Tube Arrangement:
If the rows of tubes are closely spaced (i.e., ), the flow over the tubes in subsequent rows is influenced by the tubes in the previous rows. This interaction affects the heat transfer coefficient, particularly in the first few rows. Typically, after about ten rows, the flow pattern stabilizes, and the average convective heat transfer coefficient becomes relatively constant. Heat Transfer Correlations:
For practical calculations, empirical correlations are often used to estimate the Nusselt number, which helps in determining the average convective heat transfer coefficient. A common correlation form is:
where and are constants determined empirically, is the Reynolds number based on the diameter of the tube, and is the Prandtl number.
Forced convection is an essential mechanism for enhancing heat transfer in various engineering applications. By understanding key parameters such as the Nusselt number, Reynolds number, and Prandtl number, as well as the influence of tube arrangement in heat exchangers, engineers can optimize designs for efficient heat transfer. Empirical correlations and theoretical principles provide a foundation for practical calculations, ensuring effective thermal management in systems involving forced convection.
SAMPLE PROBLEM:
A heat exchanger, with staggered tubes as shown in the figure, is used to heat atmospheric air entering at 5 °C. The temperature of the surface of the tubes is maintained at 100 °C with steam condensing inside the tubes other details of the heat exchanger are:
Determine: - The exit temperature of the air .
- Heat transfer rate
- The fan power required to maintain the air flow.
Correlations for Banks of Tubes 0.7<Pr<500 Number of rows ≥ 16 a=ST/d, b=S1/d (see Figure)
Thermodynamic Properties of Gases at Atmospheric Pressure
Computing Fan Power Required to Overcome Friction Resistance in Tubes
In systems where fluid flows through a network of tubes or a heat exchanger, overcoming frictional resistance is crucial. This frictional resistance is typically managed by fans or pumps. To determine the power required for this purpose, we need to analyze the energy balance and pressure drop across the system. Energy Equation for a Control VolumeFor a reversible flow situation, the energy balance can be simplified. Considering the following energy equation:
Where: - = Specific energy at the exit
- = Specific energy at the inlet
- = Heat added or removed
- = Mass flow rate
If the velocity at the inlet () is very small (which is achievable by placing the control surface far from the fan where free-stream conditions prevail) and the change in potential energy is negligible, the energy equation simplifies to:
Where: - = Fan power required
- = Inlet pressure
- = Exit pressure
- = Density of the fluid
- = Exit velocity of the fluid
In practical terms: - = Atmospheric pressure (pressure at the exit of the heat exchanger)
Pressure Drop CalculationThe pressure drop () across the heat exchanger or tube bank can be calculated using the following formula:
Where: - = Pressure at the inlet of the tube bank
- = Pressure at the outlet of the tube bank
- = Number of tubes
- = Empirical constant (related to the tube arrangement)
- = Density of the fluid
- = Maximum fluid velocity
- = Friction factor
Friction Factor for Tube Banks
From the given parameters:
Substitute these values into the pressure drop formula:
Fan Power CalculationUsing the simplified energy equation:
Given: - = Mass flow rate = 58.53 kg/s
- = 2,288 Pa
- = 1.211 kg/m³
- = 30 m/s
Substitute these values into the equation:
To overcome the friction resistance in the tubes, the fan needs to provide a power of approximately 137 kW. This calculation takes into account the pressure drop across the heat exchanger, the density of the fluid, and the exit velocity. Properly managing this power ensures efficient operation of the heat exchanger and optimal performance of the cooling or heating system.
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