/*! 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 4 A 10.0 -ft compressed-air tank i... [FREE SOLUTION] | 91Ó°ÊÓ

91Ó°ÊÓ

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.

Short Answer

Expert verified
The rate of air being added, \(\dot{n}\), can be calculated by using the Ideal Gas Law and a differential mass balance. Once we have the value of \(N(t)\), we can estimate the moles of Oxygen by considering its percentage in air. The potential inaccuracies may come from assumptions made during the calculation.

Step by step solution

01

Calculate Initial Moles of Air in the Tank

Initially, the tank is at atmospheric pressure, 1 atm. The volume of the tank \(V\) is 10 ft\(^3\). Given that the temperature \(T\) is \(72^{\circ} \mathrm{F}= 533.7^{\circ} \mathrm{R}\) (by converting to Rankine), and \(R = 10.73 \)psia.ft\(^3\)/(lbmol.R).To calculate the initial number of moles of air in the tank at \(t=0\), use the ideal-gas law equation \(PV = nRT\), Hence, \(n_{o}=PV/RT\)
02

Set Up the Differential Balance and Determine the Initial Condition

A general mass balance for a batch system can be written as\(\frac{dN}{dt} = \dot{n}\)Let \(N(t)\) be the number of lb-moles of air in the tank. The initial condition is given by \(N(0) = n_o\)
03

Integrate to Obtain \(N(t)\)

Integrating over the limits between \(0\) and \(t\) for \(N\) and with \(\dot{n}\) being constant, we can obtain \(N(t) = n_o + \dot{n}t\)
04

Estimating moles of Oxygen and Possible Inaccuracies

To estimate Oxygen, multiply \(N(t)\) by 0.21 (as Oxygen is around 21% of air). Potential inaccuracies may come from the assumption of ideal gas behavior, constant temperature, and ignoring the real composition of air.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with 91Ó°ÊÓ!

Key Concepts

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

Differential Balance
In physics and engineering, creating a balance for a system is like checking the inputs and outputs. In the context of gas in a tank, a differential balance helps us track how the amount of gas changes over time. This involves using the formula \[ \frac{dN}{dt} = \dot{n} \] which indicates that the change in the number of moles of gas, \(N(t)\), over time depends directly on the rate at which gas is being added or removed, \(\dot{n}\).
  • \(N(t)\): Total moles of gas in the tank at time \(t\).
  • \(\dot{n}\): Rate of gas addition, in moles per second.
When starting a calculation, it's crucial to define an initial state. That means we set up an equation based on the initial conditions, like the moles already in the tank at the beginning. Initial conditions provide the necessary reference point for computing how changes occur over time.
By integrating our balance formula, we can predict the amount of gas at any future time \(t\), given the rate \(\dot{n}\) and initial moles \(n_0\). This gives us the formula: \[ N(t) = n_0 + \dot{n}t \] This shows the accumulated gas in the tank with constant addition over time.
Mole Calculation
Mole calculations are a way to relate the physical quantities of material with their amounts at a molecular level. In our air tank context, knowing the moles tells us how much of the gas is physically present. We utilize the Ideal Gas Law formula to relate pressure \(P\), volume \(V\), and temperature \(T\) to the number of moles \(n\) using: \[ PV = nRT \] where \(R\) is the Ideal Gas Constant. Adjusting this formula, we can determine initial moles at standard conditions by solving for \(n_0\): \[ n_0 = \frac{PV}{RT} \]
  • \(P\): Pressure inside the tank initially (atmospheric conditions).
  • \(V\): Volume of the tank.
  • \(R\): Ideal Gas Constant, a fixed value that correlates the other variables.
  • \(T\): Temperature in Rankine for calculations.
The ability to perform mole calculations allows us to determine precise amounts of gas, essential for ensuring the correct functioning of processes involving gases. This step is foundational when dealing with gases in controlled environments.
Gas Behavior Assumptions
When studying gases like air in a tank, scientists often assume ideal behavior to simplify calculations. The Ideal Gas Law assumes that gas molecules do not attract or repel each other and have no volume themselves. These assumptions allow the simplified equation \[ PV = nRT \] to accurately predict gas behavior at standard conditions.
However, in real-world situations, gas behavior can deviate slightly from these assumptions, especially under extreme temperatures or pressures. This is due to:
  • Real gas particles occupying space and having volume.
  • Intermolecular forces which can affect movement and pressure.
In our tank problem, these assumptions make it easier to calculate and conceptualize the air's behavior, provided conditions remain near standard. Deviations from ideal behavior are generally small, but should be considered in precise applications. Despite potential inaccuracies, the ideal assumptions are valuable for quick and effective solution approximations in many situations.

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

A steam coil is immersed in a stirred tank. Saturated steam at 7.50 bar condenses within the coil, and the condensate emerges at its saturation temperature. A solvent with a heat capacity of \(2.30 \mathrm{kJ} /\left(\mathrm{kg} \cdot^{\cdot} \mathrm{C}\right)\) is fed to the tank at a steady rate of \(12.0 \mathrm{kg} / \mathrm{min}\) and a temperature of \(25^{\circ} \mathrm{C},\) and the heated solvent is discharged at the same flow rate. The tank is initially filled with \(760 \mathrm{kg}\) of solvent at \(25^{\circ} \mathrm{C},\) at which point the flows of both steam and solvent are commenced. The rate at which heat is transferred from the steam coil to the solvent is given by the expression $$\dot{Q}=U A\left(T_{\mathrm{steam}}-T\right)$$ where \(U A\) (the product of a heat transfer coefficient and the coil surface area through which the heat is transferred) equals \(11.5 \mathrm{kJ} /\left(\min \cdot^{\circ} \mathrm{C}\right) .\) The tank is well stirred, so that the temperature of the contents is spatially uniform and equals the outlet temperature. (a) Prove that an energy balance on the tank contents reduces to the equation given below and supply an initial condition. \frac{d T}{d t}=1.50^{\circ} \mathrm{C} / \mathrm{min}-0.0224 T (b) Without integrating the equation, calculate the steady-state value of \(T\) and sketch the expected plot of \(T\) versus \(t,\) labeling the values of \(T_{\mathrm{b}}\) at \(t=0\) and \(t \rightarrow \infty\) (c) Integrate the balance equation to obtain an expression for \(T(t)\) and calculate the solvent temperature after 40 minutes. (d) The tank is shut down for routine maintenance, and a technician notices that a thin mineral scale has formed on the outside of the steam coil. The coil is treated with a mild acid that removes the scale and reinstalled in the tank. The process described above is run again with the same steam conditions, solvent flow rate, and mass of solvent charged to the tank, and the temperature after 40 minutes is \(55^{\circ} \mathrm{C}\) instead of the value calculated in Part (c). One of the system variables listed in the problem statement must have changed as a result of the change in the stirrer. Which variable would you guess it to be, and by what percentage of its initial value did it change?

An electrical coil is used to heat \(20.0 \mathrm{kg}\) of water in a closed well-insulated vessel. The water is initially at \(25^{\circ} \mathrm{C}\) and 1 atm. The coil delivers a steady \(3.50 \mathrm{kW}\) of power to the vessel and its contents. (a) Write a differential energy balance on the water, assuming that \(97 \%\) of the energy delivered by the coil goes into heating the water. What happens to the other \(3 \% ?\) (b) Integrate the equation of Part (a) to derive an expression for the water temperature as a function of time. (c) How long will it take for the water to reach the normal boiling point? Will it boil at this temperature? Explain your answer.

A ventilation system has been designed for a large laboratory with a volume of \(1100 \mathrm{m}^{3}\). The volumetric flow rate of ventilation air is \(700 \mathrm{m}^{3} / \mathrm{min}\) at \(22^{\circ} \mathrm{C}\) and 1 atm. (The latter two values may also be taken as the temperature and pressure of the room air.) A reactor in the laboratory is capable of emitting as much as 1.50 mol of sulfur dioxide into the room if a seal ruptures. An \(\mathrm{SO}_{2}\) mole fraction in the room air greater than \(1.0 \times 10^{-6}(1 \mathrm{ppm})\) constitutes a health hazard. (a) Suppose the reactor seal ruptures at a time \(t=0,\) and the maximum amount of \(\mathrm{SO}_{2}\) is emitted and spreads uniformly throughout the room almost instantaneously. Assuming that the air flow is sufficient to make the room air composition spatially uniform, write a differential SO_ balance, letting \(N\) be the total moles of gas in the room (assume constant) and \(x(t)\) the mole fraction of \(\mathrm{SO}_{2}\) in the laboratory air. Convert the balance into an equation for \(d x / d t\) and provide an initial condition. (Assume that all of the \(\left.\mathrm{SO}_{2} \text { emitted is in the room at } t=0 .\right)\) (b) Predict the shape of a plot of \(x\) versus \(t\). Explain your reasoning, using the equation of Part (a) in your explanation. (c) Separate variables and integrate the balance to obtain an expression for \(x(t)\). Check your solution. (d) Convert the expression for \(x(t)\) into an expression for the concentration of \(\mathrm{SO}_{2}\) in the room, \(C_{\mathrm{SO}_{2}}\) (mol \(\mathrm{SO}_{2} / \mathrm{L}\) ). Calculate (i) the concentration of \(\mathrm{SO}_{2}\) in the room two minutes after the rupture occurs, and (ii) the time required for the \(S O_{2}\) concentration to reach the "safe" level. (e) Why would it probably not yet be safe to enter the room after the time calculated in Part (d)? (Hint:One of the assumptions made in the problem is probably not a good one.)

A 2000 -liter tank initially contains 400 liters of pure water. Beginning at \(t=0\), an aqueous solution containing \(1.00 \mathrm{g} / \mathrm{L}\) of potassium chloride flows into the tank at a rate of \(8.00 \mathrm{L} / \mathrm{s}\) and an outlet stream simultaneously starts flowing at a rate of \(4.00 \mathrm{L} / \mathrm{s}\). The contents of the tank are perfectly mixed, and the densities of the feed stream and of the tank solution, \(\rho(g / L),\) may be considered equal and constant. Let \(V(t)(\mathrm{L})\) denote the volume of the tank contents and \(C(t)(\mathrm{g} / \mathrm{L})\) the concentration of potassium chloride in the tank contents and outlet stream. (a) Write a balance on total mass of the tank contents, convert it to an equation for \(d V / d t\), and provide an initial condition. Then write a potassium chloride balance, show that it reduces to $$\frac{d C}{d t}=\frac{8-8 C}{V}$$ and provide an initial condition. (Hint: You will need to use the mass balance expression in your derivation.) (b) Without solving either equation, sketch the plots you expect to obtain for \(V\) versus \(t\) and \(C\) versus \(t\) If the plot of \(C\) versus \(t\) has an asymptotic limit as \(t \rightarrow \infty,\) determine what it is and explain why it makes sense. (c) Solve the mass balance to obtain an expression for \(V(t)\). Then substitute for \(V\) in the potassium chloride balance and solve for \(C(t)\) up to the point when the tank overflows. Calculate the \(\mathrm{KCl}\) concentration in the tank at that point.

Ninety kilograms of sodium nitrate is dissolved in \(110 \mathrm{kg}\) of water. When the dissolution is complete (at time \(t=0\) ), pure water is fed to the tank at a constant rate \(\dot{m}(\mathrm{kg} / \mathrm{min}),\) and solution is withdrawn from the tank at the same rate. The tank may be considered perfectly mixed. (a) Write a total mass balance on the tank and use it to prove that the total mass of liquid in the tank remains constant at its initial value. (b) Write a balance on sodium nitrate, letting \(x(t, \dot{m})\) equal the mass fraction of \(\mathrm{NaNO}_{3}\) in the tank and outlet stream. Convert the balance into an equation for \(d x / d t\) and provide an initial condition. (c) On a single graph of \(x\) versus \(t,\) sketch the shapes of the plots you would expect to obtain for \(\dot{m}=50 \mathrm{kg} / \mathrm{min}, 100 \mathrm{kg} / \mathrm{min},\) and \(200 \mathrm{kg} / \mathrm{min} .\) (Don't do any calculations.) Explain your reason- ing, using the equation of Part (b) in your explanation. (d) Separate variables and integrate the balance to obtain an expression for \(x(t, \dot{m})\). Check your solution. Then generate the plots of \(x\) versus \(t\) for \(\dot{m}=50 \mathrm{kg} / \mathrm{min}, 100 \mathrm{kg} / \mathrm{min},\) and \(200 \mathrm{kg} / \mathrm{min}\) and show them on a single graph. (A spreadsheet is a convenient tool for carrying out this step.) (e) If \(\dot{m}=100 \mathrm{kg} / \mathrm{min}\), how long will it take to flush out \(90 \%\) of the sodium nitrate originally in the tank? How long to flush out 99\%? 99.9\%? (f) The stream of water enters the tank at a point near the top, and the exit pipe from the tank is located on the opposite side toward the bottom. One day the plant technician forgot to turn on the mixing impeller in the tank. On the same chart, sketch the shapes of the plots of \(x\) versus \(t\) you would expect to see with the impeller on and off, clearly showing the differences between the two curves at small values and large values of \(t .\) Explain your reasoning.

See all solutions

Recommended explanations on Chemistry Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.