/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 31 A steam radiator is used to heat... [FREE SOLUTION] | 91Ó°ÊÓ

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A steam radiator is used to heat a \(60-\mathrm{m}^{3}\) room. Saturated steam at 3.0 bar condenses in the radiator and emerges as a liquid at the saturation temperature. Heat is lost from the room to the outside at a rate $$\dot{Q}(\mathrm{kJ} / \mathrm{h})=30.0\left(T-T_{0}\right)$$ where \(T\left(^{\circ} \mathrm{C}\right)\) is the room temperature and \(T_{0}=0^{\circ} \mathrm{C}\) is the outside temperature. At the moment the radiator is turned on, the temperature in the room is \(10^{\circ} \mathrm{C}\). (a) Let \(\dot{m}_{\mathrm{s}}(\mathrm{kg} / \mathrm{h})\) denote the rate at which steam condenses in the radiator and \(n(\mathrm{kmol})\) the quantity of air in the room. Write a differential energy balance on the room air, assuming that \(n\) remains constant at its initial value, and evaluate all numerical coefficients. Take the heat capacity of air \(\left(C_{v}\right)\) to be constant at \(20.8 \mathrm{J} /\left(\mathrm{mol} \cdot^{\circ} \mathrm{C}\right)\) (b) Write the steady-state energy balance on the room air and use it to calculate the steam condensation rate required to maintain a constant room temperature of \(24^{\circ} \mathrm{C}\). Without integrating the transient balance, sketch a plot of \(T\) versus \(t,\) labeling both the initial and maximum values of \(T\) (c) Integrate the transient balance to calculate the time required for the room temperature to rise by \(99 \%\) of the interval from its initial value to its steady-state value, assuming that the steam condensation rate is that calculated in Part (b).

Short Answer

Expert verified
The solution involves conducting energy balance analyses, calculating steam condensation rate for a constant room temperature, and integrating the energy balance equation to find out the time required for the room temperature to increase by 99% of the total increase. However, the specific numerical coefficients and final results would depend on the values of various given and derived properties.

Step by step solution

01

Write a differential energy balance

Due to the conservation of energy principle, the rate of energy increase within the room comes from heat added through condensation minus the heat loss towards the outside. You can express this mathematically as:\[ \frac{d\left(nCvT\right)}{dt} = \dot{m}_{\text{s}}h_{\text{fg}} - \dot{Q} \]where \(d\left(nCvT\right)/dt\) is the rate of energy increase in the room, \( \dot{m}_{\text{s}}h_{\text{fg}}\) represents the heat added to the room through condensation (with \(\dot{m}_{\text{s}}\) being the mass flow rate of the condensing steam and \(h_{\text{fg}}\) its heat of vaporization), and \(\dot{Q}\) accounts for the heat loss towards outside. Equating the given value of \(\dot{Q}\), you get:\[ \frac{d\left(nCvT\right)}{dt} = \dot{m}_{\text{s}}h_{\text{fg}} - 30.0\left(T-T_{0}\right) \]Here, \(t\) is the time, \(n\) is the quantity of air in the room, \(Cv\) is the heat capacity of air, \(T\) is the room temperature, and \(T_{0}\) is the outside temperature.
02

Write the steady-state energy balance and calculate steam condensation rate

The steady state is reached when the room temperature doesn't change, indicating that the rates of heat entering and displacement are equal. Therefore, \( \frac{d\left(nCvT\right)}{dt} = 0 \), so the energy balance equation becomes:\[ \dot{m}_{\text{s}}h_{\text{fg}} = 30.0\left(T_{\text{ss}}-T_{0}\right) \]This equation lets you find the steam condensation rate, \( \dot{m}_{\text{s}} \), required to maintain a constant room temperature (\( T_{\text{ss}} = 24°C \)). You would divide the right side of the equation by \( h_{\text{fg}} \).
03

Calculate the time for room temperature to rise by 99%

To find the time required (\( t_{\text{99}} \)) for the room temperature to rise by 99% of the interval from its initial value to its steady-state value, integrate the transient energy balance equation over time and temperature. Rearrange the equation by isolating \( dt \) and integrate it from \( t = 0 \) to \( t = t_{\text{99}} \) and \( T = T_{\text{i}} \) to \( T = 0.99 * (T_{\text{ss}} - T_{\text{i}}) + T_{\text{i}} \).

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Key Concepts

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

Steady-State Energy Balance
In the context of chemical processes, a steady-state energy balance is fundamental for understanding how systems reach thermal equilibrium. When a system arrives at a steady-state condition, it means that all the temperatures within the system are constant over time—even though energy may still flow in and out. This is a common scenario in industrial processes, where continuous operations aim for a consistent output.

Applying the steady-state assumption to the steam radiator scenario simplifies the problem significantly. The energy balance equation \( \dot{m}_{\text{s}}h_{\text{fg}} = 30.0\left(T_{\text{ss}}-T_{0}\right) \) reveals exactly how much steam must condense to maintain the desired room temperature. The term \( \dot{m}_{\text{s}} \) represents the condensation rate of steam within the radiator, \( h_{\text{fg}} \) is the latent heat released during condensation, and \( 30.0\left(T_{\text{ss}}-T_{0}\right) \) is the rate of heat loss from the room to the environment. Hence, the condensation rate can be determined to ensure that heat inflow matches the outflow, keeping the room temperature constant at \( 24^\circ C \).

Transient Energy Balance
Contrary to the steady-state, a transient energy balance considers the time-dependent aspects of a thermal system. This balance is crucial when analyzing how a system's temperature changes over time before reaching the steady state. Transience can complicate calculations because it requires integrating variables over a period until equilibrium is achieved.

In our radiator example, the transient energy balance comes into play right when the radiator begins to warm the room. Mathematically, this involves integrating the differential equation \( \frac{d(nC_vT)}{dt} = \dot{m}_{\text{s}}h_{\text{fg}} - 30.0(T-T_{0}) \). The left side of this equation expresses the rate at which room air energy changes due to thermal interactions. By integrating, we can predict how long it will take for the room to reach a certain percentage of its final steady-state temperature, considering the rate of steam condensation determined in the steady-state energy balance. For instance, to rise by 99% toward steady-state affairs, one would solve for \( t_{\text{99}} \) in the context of this equation.
Heat Capacity
Heat capacity is an intrinsic property that measures how much thermal energy a substance can store. It plays a significant role in calculating energy balances as it helps us understand how much energy is required to raise the temperature of a specific amount of matter by one-degree Celsius (or one Kelvin). Specifically, a substance with high heat capacity can absorb a lot of heat without experiencing a significant rise in temperature.

In our exercise, the heat capacity of the room air \( (C_v) \) is a crucial component of the differential energy balance. It influences how quickly the room heats up, given a certain rate of steam condensation. For example, because air has a relatively low heat capacity, a given amount of energy can raise the room temperature fairly quickly. This is represented by the constant \(20.8 \mathrm{J} / (\mathrm{mol} \cdot^\circ \mathrm{C})\) provided in the problem, allowing us to calculate the rate of temperature change over time given varying conditions and energy input rates.

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Most popular questions from this chapter

A tracer is used to characterize the degree of mixing in a continuous stirred tank. Water enters and leaves the mixer at a rate of \(\dot{V}\left(\mathrm{m}^{3} / \mathrm{min}\right) .\) Scale has built up on the inside walls of the tank, so that the effective volume \(V\left(\mathrm{m}^{3}\right)\) of the tank is unknown. At time \(t=0,\) a mass \(m_{0}(\mathrm{kg})\) of the tracer is injected into the tank and the tracer concentration in the outlet stream, \(C\left(\mathrm{kg} / \mathrm{m}^{3}\right),\) is monitored. (a) Write a differential balance on the tracer in the tank in terms of \(V, C,\) and \(\dot{V},\) assuming that the tank contents are perfectly mixed, and convert the balance into an equation for \(d C / d t\). Provide an initial condition, assuming that the injection is rapid enough so that all of the tracer may be considered to be in the tank at \(t=0 .\) Without doing any calculations, sketch a plot of \(C\) versus \(t\) labeling the value of \(C\) at \(t=0\) and the asymptotic value at \(t \rightarrow \infty\) (b) Integrate the balance to prove that $$C(t)=\left(m_{0} / V\right) \exp (-\dot{V} t / V)$$ (c) Suppose the flow rate through the mixer is \(\dot{V}=30.0 \mathrm{m}^{3} / \mathrm{min}\) and that the following data are taken: (For example, at \(t=1\) min, \(C=0.223 \times 10^{-3} \mathrm{kg} / \mathrm{m}^{3}\).) Verify graphically that the tank is functioning as a perfect mixer- -that is, that the expression of Part (b) fits the data- -and determine the effective volume \(V\left(\mathrm{m}^{3}\right)\) from the slope of your plot. (d) A solution of a radioactive element with a fairly short half-life (see Problem 10.16 ) is often used as a tracer for applications like the one in this problem. The advantage of doing so is that the concentration of the tracer at the outlet can be measured with a sensitive radiation detector mounted outside the exit pipe rather than having to draw fluid samples from the pipe and analyze them. What is a potential drawback of radiotracers? Why is it important that the half-life of the tracer be neither too short nor too long?

A 10.0 -ft compressed-air tank is being filled. Before the filling begins, the tank is open to the atmosphere. The reading on a Bourdon gauge mounted on the tank increases linearly from an initial value of 0.0 to 100 psi after 15 seconds. The temperature is constant at \(72^{\circ} \mathrm{F}\), and atmospheric pressure is 1 atm. (a) Calculate the rate \(\dot{n}\) (lb-mole/s) at which air is being added to the tank, assuming ideal-gas behavior. (Suggestion: Start by calculating how much is in the tank at \(t=0 .)\) (b) Let \(N(t)\) equal the number of Ib-moles of air in the tank at any time. Write a differential balance on the air in the tank in terms of \(N\) and provide an initial condition. (c) Integrate the balance to obtain an expression for \(N(t)\). Check your solution two ways. (d) Estimate the Ib-moles of oxygen in the tank after two minutes. List reasons your answer might be inaccurate, assuming there are no mistakes in your calculation.

Methane is generated via the anaerobic decomposition (biological degradation in the absence of oxygen) of solid waste in landfills. Collecting the methane for use as a fuel rather than allowing it to disperse into the atmosphere provides a useful supplement to natural gas as an energy source. If a batch of waste with mass \(M\) (tonnes) is deposited in a landfill at \(t=0,\) the rate of methane generation at time \(t\) is given by $$\dot{V}_{\mathrm{CH}_{4}}(t)=k L_{0} M_{\text {waste }} e^{-k t}$$ where \(\dot{V}_{\mathrm{CH}_{4}}\) is the rate at which methane is generated in standard cubic meters per year, \(k\) is a rate constant, \(L_{0}\) is the total potential yield of landfill gas in standard cubic meters per tonne of waste, and \(M_{\text {watte is the tonnes of waste in the landfill at } t=0}\). (a) Starting with Equation 1, derive an expression for the mass generation rate of methane, \(\dot{M}_{\mathrm{CH}_{4}}(t)\) Without doing any calculations, sketch the shape of a plot of \(M_{\mathrm{CH}, \text { versus } t \text { from } t=0 \text { to } t=3 \mathrm{y},}\) and graphically show on the plot the total masses of methane generated in Years \(1,2,\) and \(3 .\) Then derive an expression for \(M_{\mathrm{CH}_{4}}(t),\) the total mass of methane (tonnes) generated from \(t=0\) to a time \(t\) (b) A new landfill has a yield potential \(L_{0}=100\) SCM CH \(_{4}\) /tonne waste and a rate constant \(k=0.04 \mathrm{y}^{-1} .\) At the beginning of the first year, 48,000 tonnes of waste are deposited in the landfill. Calculate the tonnes of methane generated from this deposit over a three-year period. (c) A colleague solving the problem of Part (b) calculates the methane produced in three years from the \(4.8 \times 10^{4}\) tonnes of waste as $$M_{\mathrm{CH}_{4}}(t=3)=\dot{M}_{\mathrm{CH}_{4}}(t=0) \times 1 \mathrm{y}+\dot{M}_{\mathrm{CH}_{4}}(t=1) \times 1 \mathrm{y}+\dot{M}_{\mathrm{CH}_{4}}(t=2) \times 1 \mathrm{y}$$ where \(\dot{M}_{\mathrm{CH}_{4}}\) is the first expression derived in Part (a). Briefly state what has been assumed about the rate of methane generation. Calculate the value determined with this method and the percentage error in the calculation. Show graphically what the calculated value corresponds to on another sketch of \(M_{\mathrm{CH}_{4}}\) versus \(t\) (d) The following amounts of waste are deposited in the landfill on January 1 in each of three consecutive years. Exploratory Exercises - Research and Discover (e) Explain in your own words the benefits of reducing the release of methane from landfills and of using the methane as a fuel instead of natural gas. (f) One way to avoid the environmental hazard of methane generation is to incinerate the waste before it has a chance to decompose. What problems might this alternative process introduce?

Methanol is added to a storage tank at a rate of \(1200 \mathrm{kg} / \mathrm{h}\) and is simultaneously withdrawn at a rate \(\dot{m}_{w}(t)(\mathrm{kg} / \mathrm{h})\) that increases linearly with time. At \(t=0\) the tank contains \(750 \mathrm{kg}\) of the liquid and \(\dot{m}_{w}=750 \mathrm{kg} / \mathrm{h} .\) Five hours later \(\dot{m}_{\mathrm{w}}\) equals \(1000 \mathrm{kg} / \mathrm{h}\) (a) Calculate an expression for \(\dot{m}_{w}(t),\) letting \(t=0\) signify the time at which \(\dot{m}_{w}=750 \mathrm{kg} / \mathrm{h},\) and incorporate it into a differential methanol balance, letting \(M(\mathrm{kg})\) be the mass of methanol in the tank at any time. (b) Integrate the balance equation to obtain an expression for \(M(t)\) and check the solution two ways. (See Example 10.2-1.) For now, assume that the tank has an infinite capacity. (c) Calculate how long it will take for the mass of methanol in the tank to reach its maximum value, and calculate that value. Then calculate the time it will take to empty the tank. (d) Now suppose the tank volume is \(3.40 \mathrm{m}^{3}\). Draw a plot of \(M\) versus \(t\), covering the period from \(t=0\) to an hour after the tank is empty. Write expressions for \(M(t)\) in each time range when the function changes.

A 7.35 million gallon tank used for storing liquefied natural gas (LNG, which may be taken to be pure methane) must be taken out of service and inspected. All the liquid that can be pumped from the tank is first removed, and the tank is allowed to warm from its service temperature of about \(-260^{\circ} \mathrm{F}\) to \(80^{\circ} \mathrm{F}\) at 1 atm. The gas remaining in the tank is then purged in two steps: (1) Liquid nitrogen is sprayed gently onto the tank floor, where it vaporizes. As the cold nitrogen vapor is formed, it displaces the methane in a piston-like flow until the tank is completely filled with nitrogen. Once all the methane has been displaced, the nitrogen is allowed to warm to ambient temperature. (2) Air is blown into the tank where it rapidly and completely mixes with the nitrogen until the composition of the gas leaving the tank is very close to that of air. (a) Use the ideal-gas equation of state to estimate the densities of methane at \(80^{\circ} \mathrm{F}\) and 1 atm and of nitrogen at \(-260^{\circ} \mathrm{F}\) and 1 atm. How confident are you about the accuracy of each estimate? Explain. (b) If the density of liquid nitrogen is \(50 \mathrm{lb}_{\mathrm{m}} / \mathrm{ft}^{3}\), how many gallons will be required to displace all the methane from the tank? (c) How many cubic feet of air will be required to increase the oxygen concentration to \(20 \%\) by volume? (d) Explain the logic behind vaporizing nitrogen in the manner described. Why purge with nitrogen first as opposed to purging with air?

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