/*! 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 43 Nitric acid is a chemical interm... [FREE SOLUTION] | 91Ó°ÊÓ

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Nitric acid is a chemical intermediate primarily used in the synthesis of ammonium nitrate, which is used in the manufacture of fertilizers. The acid also is important in the production of other nitrates and in the separation of metals from ores. Nitric acid may be produced by oxidizing ammonia to nitric oxide over a platinum-rhodium catalyst, then oxidizing the nitric oxide to nitrogen dioxide in a separate unit where it is absorbed in water to form an aqueous solution of nitric acid.The reaction sequence is as follows:$$\begin{aligned} 4 \mathrm{NH}_{3}+5 \mathrm{O}_{2} & \rightarrow 4 \mathrm{NO}+6 \mathrm{H}_{2} \mathrm{O} \\\4 \mathrm{NO}+2 \mathrm{O}_{2} & \rightarrow 4 \mathrm{NO}_{2} \\\4 \mathrm{NO}_{2}+2 \mathrm{H}_{2} \mathrm{O}(\mathrm{l})+\mathrm{O}_{2} & \rightarrow 4 \mathrm{HNO}_{3}(\mathrm{aq}) \end{aligned}$$.Ammonia vapor produced by vaporizing pure liquid ammonia at 820 kPa absolute is mixed with air, and the combined stream enters the ammonia oxidation unit. Air at \(30^{\circ} \mathrm{C}, 1\) atm absolute, and \(50 \%\) relative humidity is compressed and fed to the process. A fraction of the air is sent to the cooling and hydration units, while the remainder is passed through a heat exchanger and mixed with the ammonia. The total oxygen fed to the process is the amount stoichiometrically required to convert all of the ammonia to HNO \(_{3},\) while the fraction sent to the ammonia oxidizer corresponds to the stoichiometric amount required to convert ammonia to NO.The ammonia reacts completely in the oxidizer, with \(97 \%\) forming NO and the rest forming \(\mathrm{N}_{2}\). Only a negligible amount of \(\mathrm{NO}_{2}\) is formed in the oxidizer. However, the gas leaving the oxidizer is subjected to a series of cooling and hydration steps in which the NO is completely oxidized to \(\mathrm{NO}_{2}\) which in turn combines with water (some of which is present in the gas from the oxidizer and the rest is added) to form a 55 wt\% aqueous solution of nitric acid. The product gas from the process may be taken to contain only \(\mathrm{N}_{2}\) and \(\mathrm{O}_{2}\). (a) Taking a basis of \(100 \mathrm{kmol}\) of ammonia fed to the process, calculate (i) the volumes \(\left(\mathrm{m}^{3}\right)\) of the ammonia vapor and air fed to the process using the compressibility-factor equation of state; (ii) the amount (kmol) and composition (in mole fractions) of the gas leaving the oxidation unit; (iii) the required volume of liquid water \(\left(\mathrm{m}^{3}\right)\) that must be fed to the cooling and hydration units; and (iv) the fraction of the air fed to the ammonia oxidizer. (b) Scale the results from Part (a) to a new basis of 100 metric tons per hour of 55\% nitric acid solution.(c) Nitrogen oxides (collectively referred to as \(\mathrm{NO}_{x}\) ) are a category of pollutants that are formed in many ways, including processes like that described in this problem. List the annual emission rates of the three largest sources of \(\mathrm{NO}_{x}\) emissions in your home region. What are the effects of exposure to excessive concentrations of \(\mathrm{NO}_{x} ?\) (d) A platinum-rhodium catalyst is used in ammonia oxidation. Fxplain the function of the catalyst, describe its structure, and explain the relationship of the structure to the function.

Short Answer

Expert verified
The solution to this problem involves chemical reaction analysis and the application of gas law principles. The results would depend on the specific parameters provided such as temperature, pressure, composition, and conversion.

Step by step solution

01

Calculate the volume of the ammonia vapor

The ammonia vapor volume can be calculated using the compressibility-factor equation of state \(PV = ZnRT\), where P is the pressure, V is the volume, Z is the compressibility factor, n is the moles of gas, R is the universal gas constant, and T is the temperature.
02

Determine the composition of the gas leaving the oxidation unit

In the ammonia oxidizer, 97% of the ammonia is converted to \(NO\), with the remaining 3% converting to \(N_{2}\). Mole fractions can be calculated by dividing the amount of each component by the total moles of gas, which includes the reaction products and the unreacted \(O_{2}\).
03

Calculate the required volume of liquid water

This can be calculated using the stoichiometry of the reactions involved in the cooling and hydration units, considering the conversion of \(NO_{2}\) into \(HNO_{3}\). The molar ratios from the reaction equations will be used to calculate the required moles of water, and hence the volume.
04

Determine the fraction of air fed to the ammonia oxidizer

This can be determined by using the stoichiometry of the reaction in the oxidizer, which involves ammonia and \(O_{2}\), and their molar relation.
05

Scale the results to a new basis

This can be done by converting the given basis of \(100 \, kmol\) of ammonia to 100 metric tons per hour of 55% nitric acid solution, considering the molecular weights of the substances involved.

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Key Concepts

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

Nitric Acid Production
Nitric acid, a critical chemical, is primarily produced through the oxidation of ammonia. This process is known as the Ostwald process and involves key steps that transform ammonia into nitric acid.
Initially, ammonia is oxidized to nitric oxide (NO) using a platinum-rhodium catalyst. This catalyst facilitates the reaction, making it efficient even at lower temperatures.
Subsequently, the nitric oxide is further oxidized to nitrogen dioxide (NO₂). Finally, NO₂ is absorbed in water, resulting in nitric acid (HNO₃).
This process not only supports fertilizer production but also contributes to other industries like metal refining and chemical manufacturing.
Ammonium Nitrate Synthesis
Ammonium nitrate is synthesized using nitric acid as a key component. It's a crucial ingredient in fertilizers due to its high nitrogen content, which is vital for plant growth.
In the synthesis process, ammonia gas is mixed with nitric acid. This reaction produces ammonium nitrate, a compound known for its highly soluble nature.
  • Reaction: \( ext{NH}_3 + ext{HNO}_3 \rightarrow ext{NH}_4 ext{NO}_3\)
This simple yet powerful reaction highlights the interconnectedness of chemical processes in agriculture and industry.
Catalytic Reaction Mechanisms
Catalysts play a vital role in accelerating chemical reactions without being consumed. In nitric acid production, a platinum-rhodium catalyst is essential for converting ammonia to nitric oxide.
This catalyst enables the reaction by reducing the activation energy needed. Its structure, a finely distributed metal surface, provides sites for the reaction to occur efficiently.
  • Benefits: Lower energy consumption, increased reaction speed, and higher yield.
Such catalysts are fundamental in industrial processes, driving efficiency and sustainability.
Environmental Impact of Nitrogen Oxides
Nitrogen oxides (NOâ‚“) are notable environmental pollutants derived from industrial processes like nitric acid production.
Major sources of NOâ‚“ emissions include vehicles, power plants, and industrial facilities. These pollutants contribute to smog, acid rain, and respiratory problems in humans.
  • Prevention: Adopting cleaner technologies and improving catalyst efficiency can reduce these emissions.
Tackling NOâ‚“ emissions is crucial for environmental protection and public health, aligning industry with sustainability goals.

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Most popular questions from this chapter

An aqueous solution of urea \((\mathrm{MW}=60.06)\) freezes at \(-4.6^{\circ} \mathrm{C}\) and 1 atm. Estimate the normal boiling point of the solution; then calculate the mass of urea (grams) that would have to be added to \(1.00 \mathrm{kg}\) of solution to raise the normal boiling point by \(3^{\circ} \mathrm{C}\).

Dehydration of natural gas is necessary to prevent the formation of gas hydrates, which can plug valves and other components of a gas pipeline, and also to reduce potential corrosion problems. Water removal can be accomplished as shown in the following schematic diagram: Natural gas containing \(80 \mathrm{lb}_{\mathrm{m}} \mathrm{H}_{2} \mathrm{O} / 10^{6} \mathrm{SCF}\) gas \(\left[\mathrm{SCF}=\mathrm{ft}^{3}(\mathrm{STP})\right]\) enters the bottom of an absorber at a rate of \(4.0 \times 10^{6}\) SCF/day. A liquid stream containing triethylene glycol (TEG, molecular weight \(=150.2\) ) and a small amount of water is fed to the top of the absorber. The absorber operates at 500 psia and \(90^{\circ} \mathrm{F}\). The dried gas leaving the absorber contains \(10 \mathrm{lb}_{\mathrm{m}} \mathrm{H}_{2} \mathrm{O} / 10^{6} \mathrm{SCF}\) gas. The solvent leaving the absorber, which contains all the TEG-water mixture fed to the column plus all the water absorbed from the natural gas, goes to a distillation column. The overhead product stream from the distillation column contains only liquid water. The bottoms product stream, which contains TEG and water, is the stream recycled to the absorber.(a) Draw and completely label a flowchart of this process. Calculate the mass flow rate ( \(\left(\mathrm{b}_{\mathrm{m}} / \mathrm{day}\right)\) and volumetric flow rate (ft \(^{3}\) /day) of the overhead product from the distillation column. (b) The greatest possible amount of dehydration is achieved if the gas leaving the absorption column is in equilibrium with the solvent entering the column. If the Henry's law constant for water in TEG at \(90^{\circ} \mathrm{F}\) is \(0.398 \mathrm{psia} / \mathrm{mol}\) fraction, what is the maximum allowable mole fraction of water in the solvent fed to the absorber?(c) A column of infinite height would be required to achieve equilibrium between the gas and liquid at the top of the absorber. For the desired separation to be achieved in practice, the mole fraction of water in the entering solvent must be less than the value calculated in Part (b). Suppose it is \(80 \%\) of that value and the flow rate of TEG in the recirculating solvent is 37 Ib \(_{\mathrm{m}}\) TEG/lb \(_{\mathrm{m}}\) water absorbed in the column. Calculate the flow rate ( \(\left(\mathrm{b}_{\mathrm{m}} / \mathrm{day}\right)\) of the solvent stream entering the absorber and the mole fraction of water in the solvent stream leaving the absorber. (d) What is the purpose of the distillation column in the process? (Hint: Think about how the process would operate without it.)

The vapor leaving the top of a distillation column goes to a condenser in which either total or partial condensation takes place. If a total condenser is used, a portion of the condensate is returned to the top of the column as \(r e f l u x\) and the remaining liquid is taken off as the overhead product (or distillate). (See Problem 6.63.) If a partial condenser is used, the liquid condensate is returned as reflux and the uncondensed vapor is taken off as the overhead product.The overhead product from an \(n\) -butane- \(n\) -pentane distillation column is 96 mole \(\%\) butane. The temperature of the cooling fluid limits the condenser temperature to \(40^{\circ} \mathrm{C}\) or higher.(a) Using Raoult's law, estimate the minimum pressure at which the condenser can operate as a partial condenser (i.e., at which it can produce liquid for reflux) and the minimum pressure at which it can operate as a total condenser. In terms of dew point and bubble point, what do each of these pressures represent for the given temperature?(b) Suppose the condenser operates as a total condenser at \(40^{\circ} \mathrm{C}\), the production rate of overhead product is \(75 \mathrm{kmol} / \mathrm{h}\), and the mole ratio of reflux to overhead product is \(1.5: 1 .\) Calculate the molar flow rates and compositions of the reflux stream and the vapor feed to the condenser.(c) Suppose now that a partial condenser is used, with the reflux and overhead product in equilibrium at \(40^{\circ} \mathrm{C}\) and the overhead product flow rate and reflux-to-overhead product ratio having the values given in Part (b). Calculate the operating pressure of the condenser and the compositions of the reflux and vapor feed to the condenser.

A gas containing nitrogen, benzene, and toluene is in equilibrium with a liquid consisting of 35 mole\% benzene and 65 mole \(\%\) toluene at \(85^{\circ} \mathrm{C}\) and 10 atm. Estimate the gas composition (mole fractions) using Raoult's law and assuming ideal-gas behavior.

The solubility coefficient of a gas may be defined as the number of cubic centimeters (STP) of the gas that dissolves in \(1 \mathrm{cm}^{3}\) of a solvent under a partial pressure of 1 atm. The solubility coefficient of \(\mathrm{CO}_{2}\) in water at \(20^{\circ} \mathrm{C}\) is \(0.0901 \mathrm{cm}^{3} \mathrm{CO}_{2}(\mathrm{STP}) / \mathrm{cm}^{3} \mathrm{H}_{2} \mathrm{O}(\mathrm{l})\). (a) Calculate the Henry's law constant in atm/mole fraction for \(\mathrm{CO}_{2}\) in \(\mathrm{H}_{2} \mathrm{O}\) at \(20^{\circ} \mathrm{C}\) from the given solubility coefficient. (b) How many grams of \(\mathrm{CO}_{2}\) can be dissolved in a \(12-\mathrm{oz}\) bottle of soda at \(20^{\circ} \mathrm{C}\) if the gas above the soda is pure \(\mathrm{CO}_{2}\) at a gauge pressure of 2.5 atm ( 1 liter \(=33.8\) fluid ounces)? Assume the liquid properties are those of water. (c) What volume would the dissolved \(C O_{2}\) occupy if it were released from solution at body temperature and pressure \(-37^{\circ} \mathrm{C}\) and 1 atm?

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