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A system consists of a body in which heat is continuously generated at a rate \(\underline{Q}_{v}\), while heat is lost from the body to its surroundings by convection. Using the lumped thermal capacity model, derive the differential equation governing the temperature response of the body. If the body is at temperature \(T_{o}\) when time \(t=0\), solve the differential equation to obtain \(T(t) .\) Also determine the steady-state temperature.

Short Answer

Expert verified
The differential equation is \( mc\frac{dT}{dt} = \underline{Q}_{v} - hA(T - T_a) \) with solution \( T(t) = T_a + \frac{\underline{Q}_{v}}{hA} + (T_0 - T_a - \frac{\underline{Q}_{v}}{hA})e^{-\frac{hA}{mc}t} \). Steady-state temperature is \( T_a + \frac{\underline{Q}_{v}}{hA} \).

Step by step solution

01

Understand the Lumped Thermal Capacity Model

In the lumped thermal capacity model, the entire body is assumed to have a uniform temperature distribution at any given time. Heat is generated internally at a constant rate \( \underline{Q}_{v} \) and lost to the surroundings by convection, characterized by a convective heat transfer coefficient \( h \) and the surface area \( A \).
02

Express Heat Generation and Loss Terms

The rate of heat generation within the body is \( \underline{Q}_{v} \). The rate of heat loss due to convection to the surroundings at ambient temperature \( T_a \) is \( hA(T(t) - T_a) \).
03

Formulate the Energy Balance Equation

Apply the first law of thermodynamics (conservation of energy principle) to the body: \[ \underline{Q}_{v} - hA(T(t) - T_a) = mc\frac{dT}{dt} \]where \( m \) is the mass and \( c \) is the specific heat capacity of the body.
04

Derive the Differential Equation

Rearrange the energy balance equation to get the differential equation governing the temperature response:\[ mc\frac{dT}{dt} = \underline{Q}_{v} - hA(T - T_a) \]This is a first-order linear differential equation in \( T \).
05

Solve the Differential Equation

Let's solve the equation:\[ \frac{dT}{dt} + \frac{hA}{mc}(T - T_a) = \frac{\underline{Q}_{v}}{mc} \]Introduce an integrating factor: \[ \mu(t) = e^{\left(\frac{hA}{mc}t\right)} \]Multiply through by the integrating factor and integrate both sides with respect to \( t \). After integration and applying initial condition \( T(0) = T_0 \), solve for \( T(t) \):\[ T(t) = T_a + \frac{\underline{Q}_{v}}{hA} + \left(T_0 - T_a - \frac{\underline{Q}_{v}}{hA}\right)e^{-\frac{hA}{mc}t} \]
06

Determine the Steady-State Temperature

The steady-state temperature \( T_s \) is when \( \frac{dT}{dt} = 0 \) (no further change in temperature). Setting the time derivative to zero in the energy balance equation gives:\[ \underline{Q}_{v} = hA(T_s - T_a) \]Solving for \( T_s \):\[ T_s = T_a + \frac{\underline{Q}_{v}}{hA} \]

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Key Concepts

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

Convection Heat Transfer
When a body loses heat to its surroundings, it often does so through a mechanism called convection. This occurs when heat is transferred through a fluid (which can be a liquid or gas) that moves around the body. A crucial factor in convection heat transfer is the convective heat transfer coefficient, denoted by the symbol \( h \). This coefficient represents how effectively heat is transferred from the surface of the body into the fluid.

Convection heat transfer is characterized by the equation \( q = hA(T - T_a) \), where:
  • \( q \) is the rate of heat transfer by convection,
  • \( A \) is the surface area of the body through which the heat is being transferred,
  • \( T \) is the temperature of the body,
  • \( T_a \) is the ambient temperature of the fluid.
This concept plays a vital role in systems where heat needs to be dissipated efficiently, such as in cooling systems or electronic devices. In the given exercise, it helps us understand how the body loses heat to its surroundings.
Differential Equation
The term differential equation sounds complex, but it's essentially a mathematical equation involving derivatives, which represent rates of change.

In thermodynamics, differential equations are often used to describe how temperature changes over time. The exercise employs a first-order linear differential equation to express the relationship between heat generated, heat lost, and the consequent change in temperature over time.

For the body in the exercise, this relationship is captured as:\[ mc\frac{dT}{dt} = \underline{Q}_{v} - hA(T - T_a) \]Where:
  • \( mc \frac{dT}{dt} \) represents the rate of change of thermal energy in the body,
  • \( \underline{Q}_{v} \) is the rate of heat generation inside the body,
  • \( hA(T - T_a) \) denotes the heat lost via convection.
Solving this equation helps us predict how the temperature \( T \) will evolve with time \( t \). Using an integrating factor, the solution provides an expression for \( T(t) \), unlocking our understanding of the thermal behavior of the body.
Steady-State Temperature
In thermal systems, the concept of steady-state temperature is pivotal. This is the condition when the temperature of a body remains constant over time, despite continuous heat generation and loss.

For our exercise, steady-state occurs when the rate of heat generation equals the rate of heat loss by convection. This means that the body's temperature does not change, because the amount of heat gained by the body exactly matches the heat being removed.

Mathematically, this is when the derivative \( \frac{dT}{dt} = 0 \) in the differential equation. By setting the equation:\[ \underline{Q}_{v} = hA(T_s - T_a) \]And solving for \( T_s \) (the steady-state temperature), we find:\[ T_s = T_a + \frac{\underline{Q}_{v}}{hA} \]Here, \( T_s \) is stable because the heat influx from internal generation is balanced by the outflux through convection. Understanding this helps in engineering practices where maintaining specific temperatures is crucial, like in climate control systems or process heaters.

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Most popular questions from this chapter

In a materials-processing experiment on a space station, a \(1 \mathrm{~cm}-\) diameter sphere of alloy is to be cooled from \(600 \mathrm{~K}\) to \(400 \mathrm{~K}\). The sphere is suspended in a test chamber by three jets of nitrogen at \(300 \mathrm{~K}\). The convective heat transfer coefficient between the jets and the sphere is estimated to be \(180 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\). Calculate the time required for the cooling process and the minimum quenching rate. Take the alloy density to be \(\rho=14,000 \mathrm{~kg} / \mathrm{m}^{3}\), specific heat \(c=140 \mathrm{~J} / \mathrm{kg} \mathrm{K}\), and thermal conductivity \(k=240 \mathrm{~W} / \mathrm{m} \mathrm{K}\). Since the emittance of the alloy is very small, the radiation contribution to heat loss can be ignored.

To prevent misting of the windscreen of an automobile, recirculated warm air at \(37^{\circ} \mathrm{C}\) is blown over the inner surface. The windscreen glass \((k=1.0 \mathrm{~W} / \mathrm{m} \mathrm{K})\) is 4 \(\mathrm{mm}\) thick, and the ambient temperature is \(5^{\circ} \mathrm{C}\). The outside and inside heat transfer coefficients are 70 and \(35 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\), respectively. (i) Determine the temperature of the inside surface of the glass. (ii) If the air inside the automobile is at \(20^{\circ} \mathrm{C}, 1\) atm, and \(80 \%\) relative humidity, will misting occur? (Refer to your thermodynamics text for the principles of psychrometry.)

A reactor vessel's contents are initially at \(290 \mathrm{~K}\) when a reactant is added, leading to an exothermic chemical reaction that releases heat at a rate of \(4 \times 10^{5} \mathrm{~W} / \mathrm{m}^{3}\). The volume and exterior surface area of the vessel are \(0.008 \mathrm{~m}^{3}\) and \(0.24 \mathrm{~m}^{2}\), respectively, and the overall heat transfer coefficient between the vessel contents and the ambient air at \(300 \mathrm{~K}\) is \(5 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\). If the reactants are well stirred, estimate their temperature after (i) I minute. (ii) 10 minutes. Take \(\rho=1200 \mathrm{~kg} / \mathrm{m}^{3}\) and \(c=3000 \mathrm{~J} / \mathrm{kg} \mathrm{K}\) for the reactants.

Two small blackened spheres of identical size-one of aluminum, the other of an unknown alloy of high conductivity-are suspended by thin wires inside a large cavity in a block of melting ice. It is found that it takes \(4.8\) minutes for the temperature of the aluminum sphere to drop from \(3^{\circ} \mathrm{C}\) to \(1^{\circ} \mathrm{C}\), and \(9.6\) minutes for the alloy sphere to undergo the same change. If the specific gravities of the aluminum and alloy are \(2.7\) and \(5.4\), respectively, and the specific heat of the aluminum is \(900 \mathrm{~J} / \mathrm{kg} \mathrm{K}\), what is the specific heat of the alloy?

Estimate the heating load for a building in a cold climate when the outside temperature is \(-10^{\circ} \mathrm{C}\) and the air inside is maintained at \(20^{\circ} \mathrm{C}\). The \(350 \mathrm{~m}^{2}\) of walls and ceiling are a composite of \(1 \mathrm{~cm}\)-thick wallboard \((k=0.2 \mathrm{~W} / \mathrm{m} \mathrm{K}), 10\) \(\mathrm{cm}\) of vermiculite insulation \((k=0.06 \mathrm{~W} / \mathrm{m} \mathrm{K})\), and \(3 \mathrm{~cm}\) of wood \((k=0.15 \mathrm{~W} / \mathrm{m}\) K). Take the inside and outside heat transfer coefficients as 7 and \(35 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\), respectively.

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