/*! 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

Air in industrial plants is subject to contamination by many different chemicals, and companies must monitor ambient levels of hazardous species to be sure they are below limits specified by the National Institute for Occupational Safety and Health (NIOSH). In personal breathing-zone sampling (as opposed to area sampling), workers wear devices that periodically collect air samples less than 10 inches away from their noses. Breathing-zone sampling and analysis methods for hundreds of species are set forth in the NIOSH Manual of Analytical Methods. \(^{13}\) For benzene, NIOSH specifies a recommended exposure limit (REL) of 0.1 ppm time-weighted average exposure (TWA), and the Occupational Safety and Health Administration (OSHA) permissible exposure limit (PEL) is 1.0ppm TWA. A worker in a petrolcum refinery has a personal breathing-zone sampler for benzenc clipped to her shirt collar. Following the NIOSH prescription, air is pumped through the sampler at a rate of \(0.200 \mathrm{L} / \mathrm{min}\) by a small battery-operated pump attached to the worker's belt. The sampler contains an adsorbent that removes essentially all of the benzene from the air passing through it. After several hours, the sampler is removed and sent to a lab for analysis, and the worker puts on a fresh sampler. On a particular day when the temperature is \(21^{\circ} \mathrm{C}\) and barometric pressure is \(730 \mathrm{mm}\) Hg, samples are collected during a 4-h period before lunch and a 3.5-h period after lunch. The analytical laboratory reports \(0.17 \mathrm{mg}\) of benzene in the first sample and \(0.23 \mathrm{mg}\) in the second. (a) Calculate the average benzene concentration, \(C_{\mathrm{B}}(\mathrm{ppm}),\) in the worker's breathing zone during each sampling period, where 1 ppm = 1 mol C \(_{6} \mathrm{H}_{6} / 10^{6}\) mol air. (b) The worker's TWA is the average concentration of benzene in her breathing zone during the eight hours of her shift. It is calculated by multiplying \(C_{\mathrm{B}}\) in each sampling period by the time of that period, summing the products over all periods during the shift, and dividing by the total time of the shift. Assume that the worker's exposure during the unsampled 30 minutes was zero, and calculate her TWA. (c) If the worker's exposure is above the recommended limits, what actions might the company take?

The ultimate analysis of a No. 4 fuel oil is 86.47 wt\% carbon, \(11.65 \%\) hydrogen, \(1.35 \%\) sulfur, and the balance noncombustible inerts. This oil is burned in a steam-generating furnace with \(15 \%\) excess air. The air is preheated to \(175^{\circ} \mathrm{C}\) and enters the furnace at a gauge pressure of \(180 \mathrm{mm}\) Hg. The sulfur and hydrogen in the fuel are completely oxidized to \(\mathrm{SO}_{2}\) and \(\mathrm{H}_{2} \mathrm{O} ; 5 \%\) of the carbon is oxidized to \(\mathrm{CO}\), and the balance forms \(\mathrm{CO}_{2}\) (a) Calculate the feed ratio ( \(\mathrm{m}^{3}\) air) \(/(\mathrm{kg} \text { oil })\) (b) Calculate the mole fractions (dry basis) and ppm (parts per million on a wet basis, or moles contained in \(10^{6}\) moles of the wet stack gas) of the stack-gas species that might be considered environmental hazards.

The bacteria acetobacter aceti convert ethanol to acetic acid in the presence of oxygen according to the reaction $$\mathrm{C}_{2} \mathrm{H}_{5} \mathrm{OH}+\mathrm{O}_{2} \rightarrow \mathrm{CH}_{3} \mathrm{COOH}+\mathrm{H}_{2} \mathrm{O}$$ In a continuous fermentation process, ethanol enters the top of the fermenter at a rate of \(145 \mathrm{kg} / \mathrm{h}\), and the air fed to the bottom of the fermenter is \(25 \%\) in excess of the amount required to consume all of the ethanol. A gas stream containing nitrogen and unreacted oxygen leaves the top of the fermenter, and a liquid stream containing acetic acid, water, and \(10 \%\) of the entering ethanol leaves the bottom. Assume that none of the ethanol, water, and acetic acid in the reactor is vaporized. The fermenter operates at \(30^{\circ} \mathrm{C},\) maintains a liquid \((\mathrm{SG}=0.95)\) height of \(4.5 \mathrm{m},\) and is open to the atmosphere (i.e., the pressure at the top of the fermenter is 1 atm). (a) What is the volumetric flow rate of air as it enters the bottom of the fermenter? What is the volumetric flow rate of gas leaving the top of the fermenter? (b) Assume a linear relationship between the fraction of oxygen reacted and the position of gas bubbles rising through the liquid in the fermenter: for example, half of the oxygen reacted is consumed in the bottom half of the fermenter. At the vertical midpoint of the fermenter, the average bubble diameter is \(1.5 \mathrm{mm}\). What is the average bubble diameter at the entry point of the air and as the gas leaves the liquid at the top of the fermenter?

A stream of hot dry nitrogen flows through a process unit that contains liquid acetone. A substantial portion of the acetone vaporizes and is carried off by the nitrogen. The combined gases leave the recovery unit at \(205^{\circ} \mathrm{C}\) and 1.1 bar and enter a condenser in which a portion of the acetone is liquefied. The remaining gas leaves the condenser at \(10^{\circ} \mathrm{C}\) and 40 bar. The partial pressure of acetone in the feed to the condenser is 0.100 bar, and that in the effluent gas from the condenser is 0.379 bar. Assume ideal-gas behavior. (a) Calculate for a basis of \(1 \mathrm{m}^{3}\) of gas fed to the condenser the mass of acetone condensed ( \(\mathrm{kg}\) ) and the volume of gas leaving the condenser \(\left(\mathrm{m}^{3}\right)\) (b) Suppose the volumetric flow rate of the gas leaving the condenser is \(20.0 \mathrm{m}^{3} / \mathrm{h}\). Calculate the rate (kg/h) at which acetone is vaporized in the solvent recovery unit.

Determining the value of newly located natural gas sites involves estimating the gas composition. quantity, and ease of access. For example, one report described a find of 2 trillion cubic feet of natural gas that is significantly offshore, in 20 feet of water, and at a drilled depth of 25,000 ft. (In North America and the OPEC countries, reported volumes are determined at 14.73 psia and \(60^{\circ} \mathrm{F}\).) The pressure in this find is estimated to be 750 atm, and the gas is 94 mole \(\%\) methane, \(3.5 \%\) ethane, and the balance \(\mathrm{CO}_{2}\) (a) Estimate the total Ib-moles of gas in the find. (b) Use the compressibility-factor equation of state to estimate the specific volume (ft \(^{3} /\) /b-mole) in the well. The temperature of such wells can vary depending upon a number of factors; for the purposes of this problem, assume that it is \(200^{\circ} \mathrm{C}\).

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