/*! 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 109 Various amounts of activated car... [FREE SOLUTION] | 91Ó°ÊÓ

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Various amounts of activated carbon were added to a fixed amount of raw cane sugar solution \((48 \mathrm{wt} \%\) sucrose in water) at \(80^{\circ} \mathrm{C} .\) A colorimeter was used to measure the color of the solutions, \(R,\) which is proportional to the concentration of trace unknown impurities in the solution. The following data were obtained (adapted from the reference in Footnote \(20,\) p. 652 ):$$\begin{array}{|l|r|r|r|r|r|r|} \hline \text { kg carbon/kg dry sucrose } & 0 & 0.005 & 0.010 & 0.015 & 0.020 & 0.030 \\ \hline R \text { (color units/kg sucrose) } & 20.0 & 10.6 & 6.0 & 3.4 & 2.0 & 1.0 \\ \hline\end{array}.$$ The reduction in color units is a measure of the mass of impurities (the adsorbate) adsorbed on the carbon (the adsorbent).(a) The general form of the Freundlich isotherm is $$X_{i}^{*}=K_{\mathrm{F}} c_{i}^{\beta}$$ where \(X_{i}^{*}\) is the mass of \(i\) adsorbed/mass of adsorbent and \(c_{i}\) is the concentration of \(i\) in solution. Demonstrate that the Freundlich isotherm may be formulated for the system described above as $$\vartheta=K_{\mathrm{F}}^{\prime} R^{\beta}$$ where \(\vartheta\) is the \(\%\) removal of color/[mass of carbon/mass of dissolved sucrose]. Then determine \(K_{\mathrm{F}}^{\prime}\) and \(\beta\) by fitting this expression to the given data, using one of the methods in Section \(2.7 .\) (b) Calculate the amount of carbon that would have to be added to a vat containing \(1000 \mathrm{kg}\) of the 48 wt\% sugar solution at \(80^{\circ} \mathrm{C}\) for a reduction in color content to \(2.5 \%\) of the original value.

Short Answer

Expert verified
The solution involves deriving the Freundlich isotherm for the specific system, determining the Freundlich constants using the provided data and then applying these constants to calculate the required amount of activated carbon necessary to achieve specific removal of the color content. The numerical values for the constants and required activated carbon are dependent on the obtained plot or numerical analysis from the provided data.

Step by step solution

01

Derive the Freundlich Isotherm

First, it's important to establish the Freundlich isotherm specific for this system. This means relating \(X_{i}^{*}\), the mass of impurities adsorbed per mass of carbon, to \(c_{i}\), the concentration of impurities in the solution, using the Freundlich isotherm, \(X_{i}^{*}=K_{\mathrm{F}} c_{i}^{\beta}\). Here, the concentration of impurities is represented by \(R\), the color of the solution. Similarly, \(\%\) removal of color per [mass of carbon/mass of dissolved sucrose] is equal to the mass of \(i\) adsorbed per mass of carbon (\(X_{i}^{*}\)). Therefore, for this specific system, the Freundlich isotherm is: \(\vartheta=K_{\mathrm{F}}^{\prime} R^{\beta}\).
02

Determine the Freundlich constants

The Freundlich constants \(K_{\mathrm{F}}^{\prime}\) and \(\beta\), are obtained by fitting this derived isotherm to the provided data (kg carbon/kg dry sucrose and R), using logarithmic plotting or numerical analysis methods. This equation is in the form of a power function, so it can be converted to linear form by taking the logarithm of both sides: \(\log \vartheta=\log K_{\mathrm{F}}^{\prime} + \beta \log R\). This linear form can be plotted using the provided data, with the resulting slope equal to \(\beta\) and the intercept equal to \(\log K_{\mathrm{F}}^{\prime}\). Therefore, the constants \(K_{\mathrm{F}}^{\prime}\) and \(\beta\) can be determined using this line.
03

Calculate the required activated carbon

Upon finding the constants \(K_{\mathrm{F}}^{\prime}\) and \(\beta\), use them to calculate the required amount of activated carbon necessary to achieve a desired reduction in color content to \(2.5 \%\) of the original value. This is done using the derived Freundlich isotherm, solving for \(\vartheta\) (since it's equal to activated carbon required/kg dry sucrose) when \(R\) is \(2.5\%\) of the original value, and the mass of dry sucrose is known (in this case, considering the 48 wt% sugar solution).

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Key Concepts

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

Freundlich Isotherm
The Freundlich Isotherm is an empirical equation describing how solutes interact with surfaces in adsorption processes. It is particularly useful for heterogeneous surface energies, which occur in real-life scenarios. In our exercise, the isotherm takes the form \(X_{i}^{*}=K_{\mathrm{F}} c_{i}^{\beta}\), where \(X_{i}^{*}\) is the mass of the impurities adsorbed per mass of adsorbent (carbon), and \(c_{i}\) is the concentration in the solution.
By manipulating this, we get \(\vartheta=K_{\mathrm{F}}^{\prime} R^{\beta}\), which relates to the percent color removal per mass of carbon per mass of dissolved sucrose. Here, \(\vartheta\) represents a redefined term for our system.
This transformation allows us to link impurity concentration, indicated by color (\(R\)), to how much gets adsorbed on carbon. By fitting data to this model, constants \(K_{\mathrm{F}}^{\prime}\) and \(\beta\) can be identified, essential for predicting adsorption dynamics in various scenarios.
Adsorbent
An adsorbent is a material tasked with bonding to atoms, ions, or molecules (known collectively as adsorbates) during a process called adsorption. In this context, activated carbon plays the role of the adsorbent. It’s a highly porous substance with a large surface area, which makes it effective in capturing impurities.
The active sites on the carbon interact with various contaminants in the sugar solution, including trace impurities that impact color. Activated carbon's efficiency makes it extensively used in industries for water purification, air filtration, and sugar refining.
The amount of activated carbon utilized can be directly linked to how much of the impurities—or color—in the solution are removed. This relationship is critical when applying the Freundlich isotherm to understand the system's behavior.
Trace Impurities
In processes involving solutions like our sugar mixture, trace impurities are undesired tiny particles or substances that affect quality. Despite being in low concentrations, these impurities can significantly impact the overall appearance or properties of a solution.
Here, trace impurities affect the sugar solution’s color. The use of activated carbon serves to reduce these impurities by adsorbing them onto its surface, thereby enhancing the quality and clarity of the sugar solution.
Understanding and managing trace impurities is crucial in industries such as food processing, where the purity of ingredients is vital for product safety and consumer satisfaction.
Colorimetry
Colorimetry is a technique used to determine the concentration of colored compounds in solution by measuring the light absorption's intensity. In this exercise, colorimetry assists in quantifying trace impurities in the sugar solution by examining its color.
The measurement obtained, denoted as \(R\), reflects the amount of impurities because the more color present, the higher the concentration of these impurities. This measurement provides insights into how effective the adsorbent—activated carbon—has been in cleansing the solution.
Using colorimetry helps in accurately gauging the achievement of desired purity levels in solutions, making the process critical in quality control and assurance across many industries.

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Most popular questions from this chapter

Various amino acids have utility as food additives and in medical applications. They are often synthesized by fermentation using a specific microorganism to convert a substrate (e.g., a sugar) into the desired product. Small quantities of other species also may be formed and must be removed to meet product specifications. For example, isoleucine (Ile), which has a molecular weight of \(131.2,\) is an essential amino acid \(^{16}\) produced by fermentation, and other amino acids such as leucine and valine also are found in the fermentation broth. The broth is subjected to several processing steps to remove these and other impurities, but final processing by crystallization is required to meet stringent specifications on purity. The strategy is to crystallize the hydrated acid form of Ile (Ile. \(\mathrm{HCl} \cdot \mathrm{H}_{2} \mathrm{O}\) ), whose crystals exclude other amino acids, and then to redissolve, neutralize, and crystallize the final Ile product. In a batch process designed to manufacture \(2500 \mathrm{kg}\) of Ile per batch, an aqueous feed solution containing 35 g Ile/dL and much lower concentrations of leucine and valine is fed to the final purification stages. The pH of the solution is 1.1 and its specific gravity is 1.02. The solution is heated to \(60^{\circ} \mathrm{C}\) and 35-wt\% HCl solution is added in a ratio of 0.4 kg per kg of feed. The addition of HCl causes the formation of crystals of Ile\cdotHCl\cdot \(\mathrm{H}_{2} \mathrm{O},\) and the production of these crystals is further increased by slowly lowering the temperature to \(20^{\circ} \mathrm{C}\). At the final crystallizer conditions the Ile solubility is \(5 \mathrm{g}\) Ile/ \(100 \mathrm{g}\) solution. The resulting slurry is sent to a centrifuge where the crystals are separated from the liquid solution and the crystal cake is washed with water. The solids leaving the centrifuge contain \(12 \%\) free water (i.e., not part of the crystal structure) and \(88 \%\) pure crystals of Ile\(\cdot \mathrm{HCl} \cdot \mathrm{H}_{2} \mathrm{O}\). \(\mathrm{H}_{2} \mathrm{O}\).The washed crystals "water to form a solution that is 4.0 g Ile/dL with gravity of 1.1. The solution is sent to an ion exchange unit where HCl is removed. Upon leaving the ion exchange unit the solution has a pH of about \(5.5 .\) It is sent to a second crystallizer where the temperature is gradually reduced to \(10^{\circ} \mathrm{C}\) and the Ile solubility is \(3.4 \mathrm{g} \mathrm{Ile} / 100 \mathrm{g} \mathrm{H}_{2} \mathrm{O}\). The crystals are separated from the slurry by centrifugation, washed with pure water, and sent to a dryer for final processing. (a) Construct a labeled flowchart for the process. (b) Choosing a basis of 1 kg of feed solution, estimate (i) the mass of HCl solution added to the system, (ii) the water added to redissolve the Ile.HCI. \(\mathrm{H}_{2} \mathrm{O}\) crystals, (iii) the mass of \(\mathrm{HCl}\) removed in the ion exchange unit, and (iv) the mass of final Ile product. (c) Scale the quantities calculated in Part (b) to the production rate of 2500 kg Ile/batch. (d) Estimate the active volume (in liters) of each of the crystallizers. (e) Amino acids are amphoteric, which means they can either donate or accept a proton \(\left(\mathrm{H}^{+}\right) .\) At low pH they tend to accept a proton and become acidic while at high pH they tend to donate a proton and become basic. They also are known as zwitterions because their ends are oppositely charged, even though the overall molecule is neutral. Isoleucine is reported to have an isoelectric point (pI) of 6.02 and \(\mathrm{pK}_{\mathrm{a}}\) values of 2.36 and \(9.60 .\) Look up the meaning of these terms and prepare a plot showing how these values are used in plotting the distribution of Ile between acid, zwitterionic (neutral), and basic forms as a function of pH. Explain why such a distribution is important in carrying out the separations described in the process.

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?

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.

A correlation for methane solubility in seawater \(^{13}\) is given by the equation $$\begin{aligned}\ln \beta=&-67.1962+99.1624\left(\frac{100}{T}\right)+27.9015 \ln \left(\frac{T}{100}\right) \\\&+S\left[-0.072909+0.041674\left(\frac{T}{100}\right)-0.0064603\left(\frac{T}{100}\right)^{2}\right]\end{aligned}$$.where \(\beta\) is volume of gas in \(\mathrm{mL}\) at STP per unit volume (mL) of water when the partial pressure of methane is \(760 \mathrm{mm} \mathrm{Hg}, T\) is temperature in Kelvin, and \(S\) is salinity in parts per thousand (ppt) by weight. At conditions of interest, the average salinity is 35 ppt, the temperature is \(42^{\circ} \mathrm{F}\), and the average density of seawater is \(1.027 \mathrm{g} / \mathrm{cm}^{3}\).(a) Estimate the mole fraction of methane in seawater for equilibrium at the given conditions. Use a mean molecular weight of \(18.4 \mathrm{g} / \mathrm{mol}\) for seawater. What is the Henry's law constant at this temperature and salinity? (b) What does the above equation say about the effect of \(S\) on methane solubility? (c) Use the Henry's law constant from Part (a) to estimate methane solubility at the given temperature and salinity, but 5000 ft below the ocean surface. (Hint: Estimate the pressure at that depth.)(d) At the low temperatures and high pressures associated with the depths described in Part (c), methane can combine with water to form methane hydrates, which may affect bothenergy availability and the environment. Explain (i) how such behavior would influence the results in Part (c) and (ii) how dissolution of methane in seawater might affect energy availability and the environment.

A \(50.0-\mathrm{L}\) tank contains an air-carbon tetrachloride gas mixture at an absolute pressure of \(1 \mathrm{atm}, \mathrm{a}\) temperature of \(34^{\circ} \mathrm{C},\) and a relative saturation of \(30 \% .\) Activated carbon is added to the tank to remove the \(\mathrm{CCl}_{4}\) from the gas by adsorption and the tank is then sealed. The volume of added activated carbon may be assumed negligible in comparison to the tank volume.(a) Calculate \(p_{\mathrm{CCl}_{4}}\) at the moment the tank is sealed, assuming ideal-gas behavior and neglecting adsorption that occurs prior to sealing. (b) Calculate the total pressure in the tank and the partial pressure of carbon tetrachloride at a point when half of the CCl_ initially in the tank has been adsorbed. Note: It was shown in Example \(6.7-1\) that at \(34^{\circ} \mathrm{C}\).$$X^{*}\left(\frac{\mathrm{g} \mathrm{CCl}_{4} \text { adsorbed }}{\mathrm{g} \text { carbon }}\right)=\frac{0.0762 p_{\mathrm{CCl}_{4}}}{1+0.096 p_{\mathrm{CCl}_{4}}}$$ where \(p_{\mathrm{CCl}_{4}}\) is the partial pressure (in \(\mathrm{mm} \mathrm{Hg}\) ) of carbon tetrachloride in the gas contacting the carbon.(c) How much activated carbon must be added to the tank to reduce the mole fraction of \(\mathrm{CCl}_{4}\) in the gas to 0.001?

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