/*! 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 54 The sulfur dioxide content of a ... [FREE SOLUTION] | 91Ó°ÊÓ

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The sulfur dioxide content of a stack gas is monitored by passing a sample stream of the gas through an SO_ analyzer. The analyzer reading is \(1000 \mathrm{ppm} \mathrm{SO}_{2}\) (parts per million on a molar basis). The sample gas leaves the analyzer at a rate of \(1.50 \mathrm{L} / \mathrm{min}\) at \(30^{\circ} \mathrm{C}\) and \(10.0 \mathrm{mm}\) Hg gauge and is bubbled through a tank containing 140 liters of initially pure water. In the bubbler, \(S O_{2}\) is absorbed and water evaporates. The gas leaving the bubbler is in equilibrium with the liquid in the bubbler at \(30^{\circ} \mathrm{C}\) and 1 atm absolute. The \(\mathrm{SO}_{2}\) content of the gas leaving the bubbler is periodically monitored with the \(\mathrm{SO}_{2}\) analyzer, and when it reaches \(100 \mathrm{ppm} \mathrm{SO}_{2}\) the water in the bubbler is replaced with 140 liters of fresh water.(a) Speculate on why the sample gas is not just discharged directly into the atmosphere after leaving the analyzer. Assuming that the equilibrium between \(S O_{2}\) in the gas and dissolved \(S O_{2}\) is described by Henry's law, explain why the SO_ content of the gas leaving the bubbler increases with time. What value would it approach if the water were never replaced? Explain. (The word "solubility" should appear in your explanation.)(b) Use the following data for aqueous solutions of \(\mathrm{SO}_{2}\) at \(30^{\circ} \mathrm{C}^{14}\) to estimate the Henry's law constant in units of \(\mathrm{mm}\) Hg/mole fraction:$$\begin{array}{|l|c|c|c|c|c|}\hline \mathrm{g} \mathrm{SO}_{2} \text { dissolved/ } 100 \mathrm{g}\mathrm{H}_{2} \mathrm{O}(\mathrm{l}) & 0.0 & 0.5 & 1.0 & 1.5 & 2.0 \\\\\hline p_{\mathrm{SO}_{2}}(\mathrm{mm} \mathrm{Hg}) & 0.0 & 37.1 & 83.7 &132 & 183 \\\\\hline\end{array}.$$(c) Estimate the SO_concentration of the bubbler solution (mol SO_/liter), the total moles of SO_ dissolved, and the molar composition of the gas leaving the bubbler (mole fractions of air, \(\mathrm{SO}_{2}\), and water vapor) at the moment when the bubbler solution must be changed. Make the following assumptions: \bullet. The feed and outlet streams behave as ideal gases. \bullet Dissolved SO_ is uniformly distributed throughout the liquid. ? The liquid volume remains essentially constant at 140 liters. \- The water lost by evaporation is small enough for the total moles of water in the tank to be considered constant. \- The distribution of SO_ between the exiting gas and the liquid in the vessel at any instant of time is governed by Henry's law, and the distribution of water is governed by Raoult's law (assume \(\left.x_{\mathrm{H}_{2} \mathrm{O}} \approx 1\right)\).(d) Suggest changes in both scrubbing conditions and the scrubbing solution that might lead to an increased removal of \(\mathrm{SO}_{2}\) from the feed gas.

Short Answer

Expert verified
Firstly, SO_2 gas cannot be discharged directly into environment due to its hazardous nature. It’s bubbled through water to reduce the SO_2 content. The gas leaving the bubbler has increasing SO_2 content over time because water can hold a finite amount of SO_2 as per Henry's law. The Henry's law constant calculated is approximately 26,500 mmHg. At the time of water change, the SO_2 concentration in bubbler solution is approximately 0.000017 mol/L, the total mole of SO_2 is about 0.0024 mol. The molar composition of the leaving gas is 0.9999 for air and 0.0001 for SO_2. To improve SO_2 removal, one could increase the pressure, change the water more frequently, and pick a scrubbing solution with high SO_2 absorbing capacity.

Step by step solution

01

Speculation and Explanation for the SO_2 Discharge Process

The SO_2 gas is dangerous and polluting, hence it cannot be discharged directly into the environment. The SO_2 gas bubbling through water is a process to absorb SO_2 into the water. According to Henry's law, the solubility of a gas in a liquid is directly proportional to the pressure of that gas above the liquid. Hence the SO_2 content in gas leaving the bubbler increases with time because more SO_2 is dissolved in the water due to the continuous supply from gas and the bubbler water could only hold finite amount SO_2.
02

Calculation of Henry's Law Constant

We can calculate the Henry's law constant (K_H) using following formula: K_H= p / x. From the data in table, we can select the third column where we have p=37.1mmHg and x=0.5gSO_2/100gH_2O. Convert the mass of SO_2 to mole (assume Molar mass of SO_2 =64 g/mol) we get x= 0.5g/64 g/mol = 0.0078 mol. And in 100g of H_2O there are 100/18 = 5.56 mol. So mole fraction of SO_2= 0.0078 / (0.0078+5.56) = 0.0014. Hence K_H = 37.1 / 0.0014 ~= 26,500 mmHg.
03

Calculation of SO_2 Concentration at the Point of Change

When the water needs to be changed, the concentration of SO_2 in the leaving gas is 100 ppm. That means the partial pressure of SO_2 in the leaving gas is 100*760/10^6 = 0.076mmHg. Now we can use Henry's law K_H = p / x to calculate the mole fraction of SO_2 in the bubbler solution: x = 0.076 / 26,500 ~=0.000003. So the concentration of SO_2 in the bubbler solution = 0.000003 * 5.56 ~= 0.000017 mol/liter. The total mole of SO_2 in 140 liters of water is then 0.000017 * 140 ~= 0.0024 mol. As for the molar composition of leaving gas, we have SO_2's mole fraction is 100/10^6 = 0.0001, and since the water lost by evaporation is negligible, we can assume H_2O's mole fraction is 1. Hence, air's mole fraction is 1 - 0.0001 = 0.9999.
04

Suggestions for Enhanced SO_2 Removal

To increase the efficiency of SO_2 removal, we could increase the pressure to have more SO_2 dissolve in the water according to Henry's law. More frequent water changes could also increase the SO_2 removal rates. In addition, selecting a more effective scrubbing solution which has a higher SO_2 absorbing capacity could also enhance SO_2 removal.

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Key Concepts

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

Sulfur Dioxide Removal
Sulfur dioxide (SOâ‚‚) is a harmful gas often emitted from industrial processes such as the burning of fossil fuels. Direct discharge of this pollutant into the atmosphere creates environmental issues like acid rain and respiratory problems for living beings. Therefore, it is crucial to remove or significantly reduce SOâ‚‚ before it is released into the environment. One common method used is "gas absorption," where SOâ‚‚ is absorbed into a liquid, typically water, before being emitted. This process not only reduces pollution but also helps to comply with environmental regulations.
Gas Absorption
Gas absorption involves a gas being dissolved into a liquid. In the case of sulfur dioxide removal, the SOâ‚‚ is absorbed into water. The process relies on solubility, which measures how well a gas dissolves in a liquid. The effectiveness of this process can depend on factors like the concentration of gas, temperature, and pressure. By increasing the surface area of contact between the gas and the liquid, the absorption efficiency can be improved. This technique is widely used in chemical engineering to separate or purify components within a process stream. In this scenario, once the SOâ‚‚ gas is absorbed into the water, it no longer poses a direct threat to the atmosphere.
Henry's Law
Henry's Law is essential in understanding how gases dissolve in liquids. It states that the amount of gas dissolved in a liquid is proportional to the partial pressure of the gas above the liquid. Mathematically, it is expressed as \( p = K_H \cdot x \), where \( p \) is the partial pressure of the gas, \( K_H \) is the Henry's Law constant, and \( x \) is the mole fraction of the dissolved gas in the liquid. As the concentration of SOâ‚‚ gas increases in the gas phase, more SOâ‚‚ will dissolve in the water until equilibrium is reached. However, the water can only hold a finite amount of SOâ‚‚, leading to eventual saturation where the rate of gas absorption decreases.
Solubility in Water
Solubility refers to the capacity of a particular substance, such as SOâ‚‚, to dissolve in a solvent like water. Factors that affect solubility include temperature, pressure, and the nature of the solvent. In terms of gas absorption for sulfur dioxide removal, solubility is crucial because it dictates how much of the gas can be captured from the stream. At a given temperature and pressure, solubility helps determine the necessary conditions for an effective absorption process. Increasing pressure can enhance solubility, while rising temperatures can generally decrease it. Understanding solubility is key to optimizing processes for maximum SOâ‚‚ retention in the water.

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Most popular questions from this chapter

The feed to a distillation column (sketched below) is a 45.0 mole\% \(n\) -pentane- 55.0 mole\% n-hexane liquid mixture. The vapor stream leaving the top of the column, which contains 98.0 mole\% pentane and the balance hexane, goes to a total condenser (which means all the vapor is condensed). Half of the liquid condensate is returned to the top of the column as reflux and the rest is withdrawn as overhead product (distillate) at a rate of \(85.0 \mathrm{kmol} / \mathrm{h}\). The distillate contains \(95.0 \%\) of the pentane fed to the column. The liquid stream leaving the bottom of the column goes to a reboiler. Part of the stream is vaporized; the vapor is returned to the bottom of the column as boilup, and the residual liquid is withdrawn as bottoms product.(a) Calculate the molar flow rate of the feed stream and the molar flow rate and composition of the bottoms product stream. (b) Estimate the temperature of the vapor entering the condenser, assuming that it is saturated (at its dew point) at an absolute pressure of 1 atm and that Raoult's law applies to both pentane and hexane. Then estimate the volumetric flow rates of the vapor stream leaving the column and of the liquid distillate product. State any assumptions you make. (c) Estimate the temperature of the reboiler and the composition of the vapor boilup, again assuming operation at 1 atm.(d) Calculate the minimum diameter of the pipe connecting the column and the condenser if the maximum allowable vapor velocity in the pipe is \(10 \mathrm{m} / \mathrm{s}\). Then list all the assumptions underlying the calculation of that number.

An aqueous waste stream leaving a process contains 10.0 wt\% sulfuric acid and 1 kg nitric acid per \(\mathrm{kg}\) sulfuric acid. The flow rate of sulfuric acid in the waste stream is \(1000 \mathrm{kg} / \mathrm{h}\). The acids are neutralized before being sent to a wastewater treatment facility by combining the waste stream with an aqueous slurry of solid calcium carbonate that contains 2 kg of recycled liquid per \(\mathrm{kg}\) solid calcium carbonate. (The source of the recycled liquid will be given later in the process description.) The following neutralization reactions occur in the reactor:$$\begin{array}{l} \mathrm{CaCO}_{3}+\mathrm{H}_{2} \mathrm{SO}_{4} \rightarrow \mathrm{CaSO}_{4}+\mathrm{H}_{2} \mathrm{O}+\mathrm{CO}_{2} \\ \mathrm{CaCO}_{3}+2 \mathrm{HNO}_{3} \rightarrow \mathrm{Ca}\left(\mathrm{NO}_{3}\right)_{2}+\mathrm{H}_{2} \mathrm{O}+\mathrm{CO}_{2} \end{array}$$,The sulfuric and nitric acids and calcium carbonate fed to the reactor are completely consumed. The carbon dioxide leaving the reactor is compressed to 30 atm absolute and \(40^{\circ} \mathrm{C}\) and sent elsewhere in the plant. The remaining reactor effluents are sent to a crystallizer operating at \(30^{\circ} \mathrm{C},\) at which temperature the solubility of calcium sulfate is \(2.0 \mathrm{g} \mathrm{CaSO}_{4} / 1000 \mathrm{g} \mathrm{H}_{2} \mathrm{O} .\) Calcium sulfate crystals form in the crystallizer and all other species remain in solution.The slurry leaving the crystallizer is filtered to produce (i) a filter cake containing \(96 \%\) calcium sulfate crystals and the remainder entrained saturated calcium sulfate solution, and (ii) a filtrate solution saturated with \(\mathrm{CaSO}_{4}\) at \(30^{\circ} \mathrm{C}\) that also contains dissolved calcium nitrate. The filtrate is split, with a portion being recycled to mix with the solid calcium carbonate to form the slurry fed to the reactor, and the remainder being sent to the wastewater treatment facility.(a) Draw and completely label a flowchart for this process. (b) Speculate on why the acids must be neutralized before being sent to the wastewater treatment facility.(c) Calculate the mass flow rates ( \(\mathrm{kg} / \mathrm{h}\) ) of the calcium carbonate fed to the process and of the filter cake; also determine the mass flow rates and compositions of the solution sent to the wastewater facility and of the recycle stream. (Caution: If you write a water balance around the reactor or the overall system, remember that water is a reaction product and not just an inert solvent.)(d) Calculate the volumetric flow rate ( \(L / h\) ) of the carbon dioxide leaving the process at 30 atm absolute and 40^0 C. Do not assume ideal-gas behavior. (e) The solubility of \(\mathrm{Ca}\left(\mathrm{NO}_{3}\right)_{2}\) at \(30^{\circ} \mathrm{C}\) is \(152.6 \mathrm{kg} \mathrm{Ca}\left(\mathrm{NO}_{3}\right)_{2}\) per \(100 \mathrm{kg} \mathrm{H}_{2} \mathrm{O}\). What is the maximum ratio of nitric acid to sulfuric acid in the feed that can be tolerated without encountering difficulties associated with contamination of the calcium sulfate by-product by \(\mathrm{Ca}\left(\mathrm{NO}_{3}\right)_{2} ?\)

In an attempt to conserve water and to be awarded LEED (Leadership in Energy and Environmental Design) certification, a 20,000-liter cistem has been installed during construction of a new building. The cistem collects water from an HVAC (heating, ventilation, and air-conditioning) system designed to provide 2830 cubic meters of air per minute at \(22^{\circ} \mathrm{C}\) and \(50 \%\) relative humidity after converting it from ambient conditions \(\left(31^{\circ} \mathrm{C}, 70 \% \text { relative humidity }\right) .\) The collected condensate serves as the source of water for lawn maintenance. Estimate (a) the rate of intake of air at ambient conditions in cubic feet per minute and (b) the hours of operation required to fill the cistern.

A gas mixture containing 85.0 mole \(\% \mathrm{N}_{2}\) and the balance \(n\) -hexane flows through a pipe at a rate of \(100.0 \mathrm{m}^{3} / \mathrm{h} .\) The pressure is 2.00 atm absolute and the temperature is \(100^{\circ} \mathrm{C}\). (a) What is the molar flow rate of the gas in \(\mathrm{kmol} / \mathrm{h}\) ? (b) Is the gas saturated? If not, to what temperature ( \(^{C} C\) ) would it have to be cooled at constant pressure in order to begin condensing hexane? (c) To what temperature ( \(C\) ) would the gas have to be cooled at constant pressure in order to condense \(80 \%\) of the hexane?

The separation of aromatic compounds from paraffins is essential in producing many polyesters that are used in a variety of products. When aromatics and paraffins have the same number of carbon atoms, they often have similar vapor pressures, which makes them difficult to separate by distillation. Extraction is a viable alternative, as illustrated by the following simple system.Sulfolane (an industrial solvent) and octane may be considered completely immiscible. At \(25^{\circ} \mathrm{C},\) the ratio of the mass fraction of xylene in the octane-rich phase to the mass fraction of xylene in the sulfolanerich phase is 0.25. One hundred kg of pure sulfolane are added to 100 kg of a mixture containing 75 wt\% octane and \(25 \%\) xylene, and the resulting system is allowed to equilibrate. How much xylene transfers to the sulfolane phase?

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