/*! 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 57 Ammonia is one of the chemical c... [FREE SOLUTION] | 91Ó°ÊÓ

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Ammonia is one of the chemical constituents of industrial waste that must be removed in a treatment plant before the waste can safely be discharged into a river or estuary. Ammonia is normally present in wastewater as aqueous ammonium hydroxide \(\left(\mathrm{NH}_{4}^{+} \mathrm{OH}^{-}\right) .\) A two- part process is frequently carried out to accomplish the removal. Lime (CaO) is first added to the wastewater, leading to the reaction $$\mathrm{CaO}+\mathrm{H}_{2} \mathrm{O} \rightarrow \mathrm{Ca}^{2+}+2\left(\mathrm{OH}^{-}\right)$$ The hydroxide ions produced in this reaction drive the following reaction to the right, resulting in the conversion of ammonium ions to dissolved ammonia: $$\mathrm{NH}_{4}^{+}+\mathrm{OH}^{-}=\mathrm{NH}_{3}(\mathrm{g})+\mathrm{H}_{2} \mathrm{O}(\mathrm{l})$$ Air is then contacted with the wastewater, stripping out the ammonia. (a) One million gallons per day of alkaline wastewater containing 0.03 mole \(\mathrm{NH}_{3} /\) mole ammoniafree \(\mathrm{H}_{2} \mathrm{O}\) is fed to a stripping tower that operates at \(68^{\circ} \mathrm{F}\). Air at \(68^{\circ} \mathrm{F}\) and 21.3 psia contacts the wastewater countercurrently as it passes through the tower. The feed ratio is \(300 \mathrm{ft}^{3}\) air/gal wastewater, and 93\% of the ammonia is stripped from the wastewater. Calculate the volumetric flow rate of the gas leaving the tower and the partial pressure of ammonia in this gas. (b) Briefly explain in terms a first-year chemistry student could understand how this process works. Include the equilibrium constant for the second reaction in your explanation. (c) This problem is an illustration of challenges associated with addressing undesirable releases into the environment; namely, in developing a process to prevent dumping ammonia into a waterway, the release is instead made to the atmosphere. Suppose you are to write an article for a newspaper on the installation of the process described in the beginning of this problem. Explain why the company is installing the two-part process, and then explain the ultimate fate of the ammonia. Take one of two positions - either that the release is harmless or that it jeopardizes the environment in the vicinity of the plant. since this is a newspaper article, it cannot be more than 800 words.

Short Answer

Expert verified
The volumetric flow rate of gas and the partial pressure of ammonia can be calculated using the known values for volumetric flow rate of wastewater and the proportion of ammonia it contains, temperature and pressure. The process involves conversion of harmful ammonia into less harmful substances through chemical reactions, but there might still be impact on the environment which needs further research.

Step by step solution

01

Understanding the removal process

Firstly, it's important to understand the process to be able to answer the questions. The process involves adding Lime to the wastewater which creates a reaction and forms hydroxide ions. These ions then interact with the ammonium ions leading to a production of dissolved ammonia. Air is then passed through, which strips out the ammonia.
02

Calculating flow rate and partial pressure

Given that one million gallons per day is the wastewater input, 0.03 mole NH3/mole ammonia-free water is the ammonia content and 300 ft3 air/gal is the air volume per gallon of wastewater, 93% of which is stripped from wastewater. The ammonia leaving the tower is thus \(0.03 * 1,000,000 * 0.93 = 27,900\) moles per day. The total volume of gas leaving the tower is the volume of air fed in plus the ammonia stripped out, which is \(300 * 1,000,000 = 300,000,000\) ft3. The partial pressure of ammonia in the gas can be found using the ideal gas law relation \(P = (nRT)/V\), where n = number of moles of ammonia, R = gas constant in proper units, T = absolute temperature in Kelvin, and V = total volume. Substituting known values should yield the answer.
03

Explaining the process in simple terms and its environmental impact

As far as explaining to a first-year chemistry student, make sure to focus on the basic concepts of chemical reactions and pressure, and demonstrate how the process works to take the harmful ammonia out of the wastewater and release it into the air. If writing a newspaper article, one will have to research on the impact of ammonia in the atmosphere and argue either that it is harmless or that it could be harmful, stressing the need for further treatment processes to remove it completely.

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Key Concepts

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

Ammonia Removal
Let's dive into the fascinating world of wastewater treatment, specifically, how ammonia—a compound found in industrial waste—is removed before the water is released back into the environment. Ammonia removal is crucial because if untreated, it can harm aquatic life and compromise water quality. In the scenario provided, we're dealing with alkaline wastewater containing ammonium hydroxide ((NH_4^+ OH^−)).

To kick off the removal process, lime (CaO) is added, which reacts with water to produce calcium ions (Ca^{2+}) and hydroxide ions (OH^−). The increased presence of hydroxide ions shifts the chemical equilibrium, converting ammonium ions (NH_4^+) into gas-form ammonia (NH_3) and water (H_2O). This change in the chemical state of ammonia—from ionic to gaseous form—is crucial as it allows for the subsequent separation step, where air strips away the gaseous ammonia, reducing the pollutant load in the wastewater.
Stripping Tower Operation
Moving on to the stripping tower operation, visualize it as a large column through which air and alkaline wastewater flow counter to each other—air moving upwards and water downwards. In the example, a tower is handling a massive one million gallons per day, using 300 cubic feet of air per gallon of wastewater.

During this process, the air 'grabs' the ammonia gas from the water, as the newly formed ammonia prefers to exist as a gas in air rather than remaining dissolved in water. The efficiency is impressive, with 93% of the ammonia transferred from the water to the air. This stripping process is governed by the principles of mass transfer and relies on a large contact surface area to achieve high removal rates.
Environmental Impact of Ammonia Emissions
While treating wastewater is essential for protecting waterways, the environmental impact of ammonia emissions from the treatment process cannot be ignored. Ammonia released into the air can react with other pollutants to form fine particulate matter, which is a health hazard. Additionally, when deposited onto soil or surface waters, ammonia can contribute to eutrophication—a process that leads to excessive growth of algae and a decrease in oxygen levels in water bodies adversely affecting aquatic ecosystems.

The choice of releasing ammonia into the atmosphere is a trade-off, where immediate water pollution is prevented at the cost of potential air quality issues. As such, it's essential that the stripping process in the wastewater treatment plant integrates with broader environmental management strategies to minimize the overall ecological footprint.
Chemical Reaction Equilibria
Understanding chemical reaction equilibria is crucial for comprehending how processes like ammonia stripping work. A chemical equilibrium represents a balance in a reversible reaction, where the rate of the forward reaction equals the rate of the reverse reaction. In the removal of ammonia, the addition of lime shifts the equilibrium of the reaction towards the production of ammonia gas. Equilibrium is governed by Le Chatelier’s principle, which states that a system at equilibrium will adjust to counteract the effect of a disturbance.

In our case, the presence of excess hydroxide ions 'disturbs' the equilibrium, thereby 'forcing' the reaction to produce more gas-form ammonia to re-establish balance. These equilibria are quantified by equilibrium constants, which signify the ratio of concentration of reactants to products at equilibrium. The entire concept is vital for designing processes like those in a stripping tower, ensuring the efficient removal of contaminants from wastewater.

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Most popular questions from this chapter

Steam reforming is an important technology for converting refined natural gas, which we take here to be methane, into a synthesis gas that can be used to produce a varicty of other chemical compounds. For example, consider a reformer to which natural gas and steam are fed in a ratio of 3.5 moles of steam per mole of methane. The reformer operates at 18 atm, and the reaction products leave the reformer in chemical equilibrium at \(875^{\circ} \mathrm{C}\). The steam reforming reaction is $$\mathrm{CH}_{4}+\mathrm{H}_{2} \mathrm{O} \rightleftharpoons \mathrm{CO}+3 \mathrm{H}_{2}$$ and the water-gas shift reaction also occurs in the reformer. $$\mathrm{CO}+\mathrm{H}_{2} \mathrm{O} \rightleftharpoons \mathrm{CO}_{2}+\mathrm{H}_{2}$$ The equilibrium constants for these two reactions are given by the expressions At \(875^{\circ} \mathrm{C}, K_{\mathrm{R}}=872.9 \mathrm{atm}^{2}\) and \(K \mathrm{w} \mathrm{G}=0.2482 .\) The process is to produce \(100.0 \mathrm{kmol} / \mathrm{h}\) of hydrogen. Calculate the feed rates (kmol/h) of methane and steam and the volumetric flow rate \(\left(\mathrm{m}^{3} / \mathrm{min}\right)\) of gas leaving the reformer.

A distillation column is being used to separate methanol and water at atmospheric pressure. The column temperature varies from approximately \(65^{\circ} \mathrm{C}\) at the top to \(100^{\circ} \mathrm{C}\) at the bottom. Liquid enters the top of the column and flows down to the bottom; vapor is generated in a reboiler at the bottom of the column, flows upward, and leaves at the top. The molar flow rate of vapor up the column may be assumed to be constant from top to bottom. The vapor velocity is kept below \(5.0 \mathrm{ft} / \mathrm{s}\) to keep the vapor from entraining liquid (suspending and carrying away liquid droplets). (a) Where in the column is the greatest risk of liquid entrainment? Explain your answer. (b) Assuming that the liquid flowing down the column and the column internals (equipment inside the column) occupy a negligible fraction of the column cross-sectional area, estimate the minimum column diameter if the vapor flow rate is 25.0 lb-mole/min. (c) Suppose the column is constructed with a diameter \(10 \%\) greater than that determined in Part (b). What are the vapor velocities at the top and bottom of the column if the vapor molar flow rate in both locations is 25.0 ib-mole/min? How much can the vapor molar flow rate be increased without causing liquid entrainment? (d) There is a need to increase process throughput, which would require the vapor molar flow rate to be doubled. It has been suggested that increasing the pressure in the column would allow that to be done without risking excessive liquid entrainment. Again applying a vapor velocity limit of \(5 \mathrm{ft} / \mathrm{s}\) what would the new pressure be?

During your summer vacation, you plan an epic adventure trip to scale Mt. Kilimanjaro in Tanzania. Dehydration is a great danger on such a climb, and it is essential to drink enough water to make up for the amount you lose by breathing. (a) During your pre-trip physical, your physician measured the average flow rate and composition of the gas you exhaled (expired air) while performing light activity. The results were \(11.36 \mathrm{L} / \mathrm{min}\) at body temperature (37^) C) and 1 atm, 17.08 mole\% oxygen, 3.25\% carbon dioxide, 6.12 mole\% \(\mathrm{H}_{2} \mathrm{O},\) and the balance nitrogen. The ambient (inspired) air contained 1.67 mole\% water and a negligible amount of carbon dioxide. Calculate the rate of mass lost through the breathing process (kg/day) and the volume of water in liters you would have to drink per day just to replace the water lost in respiration. Consider your lungs to be a continuous steady-state system, with input streams being inspired air and water and \(\mathrm{CO}_{2}\) transferred from the blood and output streams being expired air and \(\mathrm{O}_{2}\) transferred to the blood. Assume no nitrogen is transferred to or from the blood. (b) You made the trip to Tanzania and completed the climb to Uhuru Peak, the summit of Kilimanjaro, at an altitude of 5895 meters above sea level. The ambient temperature and pressure there averaged \(-9.4^{\circ} \mathrm{C}\) and \(360 \mathrm{mm} \mathrm{Hg},\) and the air contained \(0.46 \mathrm{mole} \%\) water. The molar flow rate of your expired air was roughly the same as it had been at sea level, and the expired air contained \(14.86 \% \mathrm{O}_{2}\) \(3.80 \% \mathrm{CO}_{2},\) and \(13.20 \% \mathrm{H}_{2} \mathrm{O} .\) Calculate the rate of mass lost (g/day) through breathing and water you would have to drink (L/day) just to replace the water lost in respiration. (c) The equality of the molar flow rates of expired air at sea level and at Uhuru Peak is due to a cancellation of effects, one of which would tend to increase the rate at higher altitudes and the other to decrease it. What are those effects? (Hint: Use the ideal-gas equation of state in your solution, and think about how the oxygen concentration at a high altitude would likely affect your breathing rate.)

A nitrogen rotameter is calibrated by feeding \(\mathrm{N}_{2}\) from a compressor through a pressure regulator, a needle valve, the rotameter, and a dry test meter, a device that measures the total volume of gas that passes through it. A water manometer is used to measure the gas pressure at the rotameter outlet. A flow rate is set using the needle valve, the rotameter reading, \(\phi\), is noted, and the change in the dry gas meter reading \((\Delta V)\) for a measured running time \((\Delta t)\) is recorded. The following calibration data are taken on a day when the temperature is \(23^{\circ} \mathrm{C}\) and barometric pressure is \(763 \mathrm{mm} \mathrm{Hg} .\) $$\begin{array}{rrr} \hline \phi & \Delta t(\min ) & \Delta V(\mathrm{L}) \\ \hline 5.0 & 10.0 & 1.50 \\ 9.0 & 10.0 & 2.90 \\ 12.0 & 5.0 & 2.00 \\ \hline \end{array}$$ (a) Prepare a calibration chart of \(\phi\) versus \(\dot{V}_{\text {sid }}\), the flow rate in standard \(\mathrm{cm}^{3} / \mathrm{min}\) equivalent to the actual flow rate at the measurement conditions. (b) Suppose the rotameter-valve combination is to be used to set the flow rate to 0.010 mol \(\mathrm{N}_{2} / \mathrm{min}\). What rotameter reading must be maintained by adjusting the valve?

Lewis \(^{12}\) describes the hazards of breathing air containing appreciable amounts of an asphyxiant (a gas that has no specific toxicity but, when inhaled, excludes oxygen from the lungs). When the mole percent of the asphyxiant in the air reaches \(50 \%,\) marked symptoms of distress appear, and at \(75 \%\) death occurs in a matter of minutes. A small storage room whose dimensions are \(2 \mathrm{m} \times 1.5 \mathrm{m} \times 3 \mathrm{m}\) contains a number of expensive and dangerous chemicals. To prevent unauthorized entry, the door to the room is always locked and can be opened with a key from either side. A cylinder of liquid carbon dioxide is stored in the room. The valve on the cylinder is faulty and some of the contents have escaped over the weekend. The room temperature is \(25^{\circ} \mathrm{C}\). (a) If the concentration of \(\mathrm{CO}_{2}\) reaches the lethal 75 mole \(\%\) level, what would be the mole percent of \(\mathrm{O}_{2} ?\) (b) How much \(\mathrm{CO}_{2}(\mathrm{kg})\) is present in the room when the lethal concentration is reached? Why would more than that amount have to escape from the cylinder for this concentration to be reached? (c) Describe a set of events that could result in a fatality in the given situation. Suggest at least two measures that would reduce the hazards associated with storage of this scemingly harmless substance.

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