/*! 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 48 The oxidation of nitric oxide ... [FREE SOLUTION] | 91Ó°ÊÓ

91Ó°ÊÓ

The oxidation of nitric oxide $$\mathrm{NO}+\frac{1}{2} \mathrm{O}_{2} \rightleftharpoons \mathrm{NO}_{2}$$ takes place in an isothermal batch reactor. The reactor is charged with a mixture containing 20.0 volume percent NO and the balance air at an initial pressure of \(380 \mathrm{kPa}\) (absolute). (a) Assuming ideal-gas behavior, determine the composition of the mixture (component mole fractions) and the final pressure (kPa) if the conversion of NO is 90\%. (b) Suppose the pressure in the reactor eventually equilibrates (levels out) at \(360 \mathrm{kPa}\). What is the equilibrium percent conversion of NO? Calculate the reaction equilibrium constant at the prevailing temperature, \(K_{p}\left[(\mathrm{atm})^{-0.5}\right]\), defined as $$K_{p}=\frac{\left(p_{\mathrm{NO}_{2}}\right)}{\left(p_{\mathrm{NO}}\right)\left(p_{\mathrm{O}_{2}}\right)^{0.5}}$$ where \(p_{i}(\mathrm{atm})\) is the partial pressure of species \(i\left(\mathrm{NO}_{2}, \mathrm{NO}, \mathrm{O}_{2}\right)\) at equilibrium. (c) Assuming that \(K_{\mathrm{p}}\) depends only on temperature, estimate the final pressure and composition in the reactor if the feed ratio of NO to \(\mathrm{O}_{2}\) and the initial pressure are the same as in \(\operatorname{Part}(\) a), but the feed to the reactor is pure \(\mathrm{O}_{2}\) instead of air. (d) Replace the partial pressures in the expression for \(K_{\mathrm{p}}\), and use the result to explain how reactor pressure influences the conversion of NO to \(\mathrm{NO}_{2}\)

Short Answer

Expert verified
The final pressure and conversion in part (a) is 344kPa and 90%, respectively. The equilibrium conversion and \(K_{p}\) in part (b) can be calculated by substituting the values into the formula. In part (c), change the feed ratio by altering the reactant to get the final pressure and conversion. For part (d), the conversion of NO will increase with an increase in the reactor's pressure.

Step by step solution

01

- Calculating composition and final pressure

For part (a), start by calculating the mole fractions of NO and O2. Given that air is roughly 21% O2 and 79% N2 by volume, the mole fraction \(X_{NO}\) is 0.2 and \(X_{O_2}\) is 0.21*0.8 = 0.168. The volume ratio between N2 and the reactants is 0.79/0.2=3.95, hence \(X_{N2}\) is 3.95*0.168=0.664. To get the final pressure, apply the ideal gas law. In this case, the number of moles decreases so pressure also decreases. If the conversion of NO is 90%, final pressure will be \(P_{final}\) = \(P_{initial} \times (1-0.9X_{NO}) = 380 \times (1-0.9 \times 0.2) = 344 kPa\).
02

- Calculating equilibrium percent conversion

For part (b), use Pfinal to find the equilibrium conversion. From the final pressure in the reactor, calculate the conversion of NO, which is \(X_{NO}\) = \(1-P_{final}/P_{initial}\) = \(1-360/380 = 0.053\). This is equivalent to a 5.3% conversion. Then, calculate the reaction equilibrium constant using the expression provided, which is \(K_{p} = (p_{NO_2})/(p_{NO}(p_{O_2})^{0.5})\). You get \(K_{p} = X_{NO_2}/(X_{NO}(X_{O_2})^{0.5})\). Substitute the expression above into Xs in the formula \(K_p\) obtain the value of \(K_p\).
03

- Calculating final pressure and composition

For part (c), maintain the same ratio of NO to O2 from part (a), but change the feed to the reactor to pure O2. This means the mole fraction of O2 will change to 0.8. Substitute the expression \(X_O2\) into the formulas provided above for the final pressure and the equilibrium percentage conversion of NO to get the results.
04

- Evaluating the influence of reactor pressure

For part (d), analyze how reactor pressure influences the conversion of NO to NO2 by looking at the expression for \(K_{p}\). This equation can be written in terms of pressure and mole fractions. Analzes the relationship between the reaction equilibrium constant (\(K_{p}\)) and the reactor pressure in terms of affecting the conversion of NO to NO2.

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.

Ideal Gas Law
The Ideal Gas Law is a fundamental principle in Chemical Reaction Engineering used to relate pressure, volume, temperature, and the number of moles of gases. The law is expressed as \( PV = nRT \), where \( P \) is pressure, \( V \) is volume, \( n \) is the number of moles, \( R \) is the universal gas constant, and \( T \) is temperature.
Understanding this relationship is crucial when dealing with gases in reactors, as it allows predictions of how the system will behave under different conditions.
  • It assumes gases behave ideally, which means their particles occupy negligible space and have no interactions except during collisions.
  • This assumption is often valid under high temperature and low-pressure conditions.
When applied, this law helps to calculate parameters like the final pressure or composition of a gas mixture after a reaction, as demonstrated in the nitric oxide oxidation problem.
By understanding the Ideal Gas Law, you'll be able to predict changes in system variables, allowing for better control and optimization of reactions.
Equilibrium Constant
The Equilibrium Constant, \( K_p \), is a vital concept that quantifies the state of a reaction at equilibrium, especially concerning pressure in gas-phase reactions.
For the reaction involving nitric oxide oxidation, \( K_p \) is defined as:\[K_{p} = \frac{(p_{NO_{2}})}{(p_{NO})(p_{O_{2}})^{0.5}}\]
At equilibrium, the forward and reverse reaction rates are equal, and the concentrations of reactants and products become constant.
  • If \( K_p \) is large, the reaction favors the formation of products at equilibrium.
  • If \( K_p \) is small, the reaction favors the reactants.
In the exercise, understanding \( K_p \) allows for the calculation of the equilibrium conversion of nitric oxide into nitrogen dioxide. It also helps demonstrate how changes in pressure or composition affect the equilibrium state.
Remember, \( K_p \) depends on temperature and can be used to predict how a reaction will shift when subjected to temperature changes.
Isothermal Batch Reactor
An Isothermal Batch Reactor is a type of chemical reactor where reactions occur at a constant temperature over a period of time.
In such reactors, the composition of the reaction mixture changes as the reaction progresses, but there is no inflow or outflow of material.
  • Maintaining constant temperature is vital because reaction rates and equilibria can be highly temperature dependent.
  • The reactants are initially charged into the reactor, and products are removed only after the reaction is concluded.
For the oxidation of nitric oxide given in the exercise, using an isothermal batch reactor ensures that the reaction dynamics, such as pressure changes and conversion rates, depend only on the initial conditions and the reaction's kinetics.
This type of reactor is ideal for reactions where a single, controlled environment is necessary to simplify analysis and optimize reaction conditions, as sharply varying external conditions could complicate the reaction outcome.
Nitric Oxide Oxidation
Nitric Oxide Oxidation is a chemical reaction where nitric oxide \( NO \) reacts with oxygen \( O_2 \) to form nitrogen dioxide \( NO_2 \).
This process is demonstrated as:\[\mathrm{NO} + \frac{1}{2} \mathrm{O}_2 \rightleftharpoons \mathrm{NO}_2\]
This reaction plays a significant role in atmospheric chemistry and industrial processes.
  • Nitric oxide is a significant pollutant emitted from vehicles and industrial activities.
  • Its oxidation to nitrogen dioxide is a critical step in forming photochemical smog.
In chemical engineering, understanding this oxidation process is crucial for pollution control and the design of reactors aimed at mitigating NO emissions.
In the context of the exercise, calculating conversions and equilibrium conditions helps illustrate how to manage chemical reactions to achieve desirable environmental outcomes.

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 stream of liquid \(n\) -pentane flows at a rate of \(50.4 \mathrm{L} / \mathrm{min}\) into a heating chamber, where it evaporates into a stream of air \(15 \%\) in excess of the amount needed to burn the pentane completely. The temperature and gauge pressure of the entering air are \(336 \mathrm{K}\) and \(208.6 \mathrm{kPa}\). The pentane-laden heated gas flows into a combustion furnace in which a fraction of the pentane is burned. The product gas, which contains all of the unreacted pentane and no \(\mathrm{CO},\) goes to a condenser in which both the water formed in the furnace and the unreacted pentane are liquefied. The uncondensed gas leaves the condenser at \(275 \mathrm{K}\) and 1 atm absolute. The liquid condensate is separated into its components, and the flow rate of the pentane is measured and found to be \(3.175 \mathrm{kg} / \mathrm{min}\). (a) Calculate the fractional conversion of pentane achieved in the furnace and the volumetric flow rates ( \(\mathrm{L} / \mathrm{min}\) ) of the feed air, the gas leaving the condenser, and the liquid condensate before its components are separated. (b) Sketch the apparatus that could have been used to separate the pentane and water in the condensate. Hint: Remember that pentane is a hydrocarbon and recall what is said about oil (hydrocarbons) and water.

Most of the concrete used in the construction of buildings, roads, dams, and bridges is made from Portland cement, a substance obtained by pulverizing the hard, granular residue (clinker) from the roasting of a mixture of clay and limestone and adding other materials to modify the setting properties of the cement and the mechanical properties of the concrete. The charge to a Portland cement rotary kiln contains \(17 \%\) of a dried building clay \(\left(72 \mathrm{wt} \% \mathrm{SiO}_{2}\right.\) \(\left.16 \% \mathrm{Al}_{2} \mathrm{O}_{3}, 7 \% \mathrm{Fe}_{2} \mathrm{O}_{3}, 1.7 \% \mathrm{K}_{2} \mathrm{O}, 3.3 \% \mathrm{Na}_{2} \mathrm{O}\right)\) and \(83 \%\) limestone \(\left(95 \mathrm{wt} \% \mathrm{CaCO}_{3}, 5 \% \text { impuritics }\right)\) When the solid temperature reaches about \(900^{\circ} \mathrm{C},\) calcination of the limestone to lime (CaO) and carbon dioxide occurs. As the temperature continues to rise to about \(1450^{\circ} \mathrm{C},\) the lime reacts with the minerals in the clay to form such compounds as \(3 \mathrm{CaO} \cdot \mathrm{SiO}_{2}, 3 \mathrm{CaO} \cdot \mathrm{Al}_{2} \mathrm{O}_{3},\) and \(4 \mathrm{CaO} \cdot \mathrm{Al}_{2} \mathrm{O}_{3} \cdot \mathrm{Fe}_{2} \mathrm{O}_{3} .\) The flow rate of \(\mathrm{CO}_{2}\) from the kiln is \(1350 \mathrm{m}^{3} / \mathrm{h}\) at \(1000^{\circ} \mathrm{C}\) and 1 atm. Calculate the feed rates of clay and limestone ( \(\mathrm{kg} / \mathrm{h}\) ) and the weight percent of \(\mathrm{Fe}_{2} \mathrm{O}_{3}\) in the final cement.

The demand for a particular hydrogenated compound, \(\mathrm{S}\), is \(5.00 \mathrm{kmol} / \mathrm{h}\). This chemical is synthesized in the gas-phase reaction $$A+H_{2}=S$$ The reaction equilibrium constant at the reactor operating temperature is $$K_{p}=\frac{p_{\mathrm{S}}}{p_{\Lambda} p_{\mathrm{H}_{2}}}=0.1 \mathrm{atm}^{-1}$$ The fresh feed to the process is a mixture of \(A\) and hydrogen that is mixed with a recycle stream consisting of the same two species. The resulting mixture, which contains \(3 \mathrm{kmol} \mathrm{A} / \mathrm{kmol} \mathrm{H}_{2},\) is fed to the reactor, which operates at an absolute pressure of 10.0 atm. The reaction products are in equilibrium. The effluent from the reactor is sent to a separation unit that recovers all of the \(S\) in essentially pure form. The A and hydrogen leaving the separation unit form the recycle that is mixed with fresh feed to the process. Calculate the feed rates of hydrogen and A to the process in kmol/h and the recycle stream flow rate in SCMH (standard cubic meters per hour).

As everyone who has used a fireplace knows, when a fire burns in a furnace, a draft, or slight vacuum, is induced that causes the hot combustion gases and entrained particulate matter to flow up and out of the stack. The reason is that the hot gas in the stack is less dense than air at ambient temperature, leading to a lower hydrostatic head inside the stack than at the furnace inlet. The theoretical draft \(D\left(\mathrm{N} / \mathrm{m}^{2}\right)\) is the difference in these hydrostatic heads; the actual draft takes into account pressure losses undergone by the gases flowing in the stack. Let \(T_{\mathrm{s}}(\mathrm{K})\) be the average temperature in a stack of height \(L(\mathrm{m})\) and \(T_{\mathrm{a}}\) the ambient temperature, and let \(M_{\mathrm{s}}\) and \(M_{\mathrm{a}}\) be the average molecular weights of the gases inside and outside the stack. Assume that the pressures inside and outside the stack are both equal to atmospheric pressure, \(P_{\mathrm{a}}\left(\mathrm{N} / \mathrm{m}^{2}\right)\) (In fact, the pressure inside the stack is normally a little lower.) (a) Use the ideal-gas equation of state to prove that the theoretical draft is given by the expression $$D\left(\mathrm{N} / \mathrm{m}^{2}\right)=\frac{P_{\mathrm{a}} L g}{R}\left(\frac{M_{\mathrm{a}}}{T_{\mathrm{u}}}-\frac{M_{\mathrm{s}}}{T_{\mathrm{s}}}\right)$$ (b) Suppose the gas in a 53 -m stack has an average temperature of \(655 \mathrm{K}\) and contains 18 mole\% \(\mathrm{CO}_{2}\) \(2 \% \mathrm{O}_{2},\) and \(80 \% \mathrm{N}_{2}\) on a day when barometric pressure is \(755 \mathrm{mm}\) Hg and the outside temperature is \(294 \mathrm{K}\). Calculate the theoretical draft \(\left(\mathrm{cm} \mathrm{H}_{2} \mathrm{O}\right)\) induced in the furnace.

An innovative engineer has invented a device to replace the hydraulic jacks found at many service stations. A movable piston with a diameter of \(0.15 \mathrm{m}\) is fitted into a cylinder. Cars are raised by opening a small door near the base of the cylinder, inserting a block of dry ice (solid \(\mathrm{CO}_{2}\) ), closing and sealing the door, and vaporizing the dry ice by applying just enough heat to raise the cylinder contents to ambient temperature \(\left(25^{\circ} \mathrm{C}\right)\). The car is subsequently lowered by opening a valve and venting the cylinder gas. The device is tested by raising a car a vertical distance of \(1.5 \mathrm{m}\). The combined mass of the piston and the car is \(5500 \mathrm{kg}\). Before the piston rises, the cylinder contains \(0.030 \mathrm{m}^{3}\) of \(\mathrm{CO}_{2}\) at ambient temperature and pressure ( 1 atm). Neglect the volume of the dry ice. (a) Calculate the pressure in the cylinder when the piston comes to rest at the desired elevation. (b) How much dry ice (kg) must be placed in the cylinder? Use the SRK equation of state for this calculation. (c) Outline how you would calculate the minimum piston diameter required for any elevation of the car to occur if the calculated amount of dry ice is added. (Just give formulas and describe the procedure you would follow- -no numerical calculations are required.)

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.