/*! 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 72 A Claus plant converts gaseous s... [FREE SOLUTION] | 91Ó°ÊÓ

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A Claus plant converts gaseous sulfur compounds to elemental sulfur, thereby eliminating emission of sulfur into the atmosphere. The process can be especially important in the gasification of coal, which contains significant amounts of sulfur that is converted to \(\mathrm{H}_{2}\) S during gasification. In the Claus process, the \(\mathrm{H}_{2}\) S-rich product gas recovered from an acid-gas removal system following the gasifier is split, with one-third going to a furnace where the hydrogen sulfide is burned at 1 atm with a stoichiometric amount of air to form SO \(_{2}\). $$\mathrm{H}_{2} \mathrm{S}+\frac{3}{2} \mathrm{O}_{2} \rightarrow \mathrm{SO}_{2}+\mathrm{H}_{2} \mathrm{O}$$ The hot gases leave the furnace and are cooled prior to being mixed with the remainder of the \(\mathrm{H}_{2}\) S-rich gases. The mixed gas is then fed to a catalytic reactor where hydrogen sulfide and \(\mathrm{SO}_{2}\) react to form elemental sulfur. $$2 \mathrm{H}_{2} \mathrm{S}+\mathrm{SO}_{2} \rightarrow 2 \mathrm{H}_{2} \mathrm{O}+3 \mathrm{S}$$ The coal available to the gasification process is 0.6 wt\% sulfur, and you may assume that all of the sulfur is converted to \(\mathrm{H}_{2} \mathrm{S}\), which is then fed to the Claus plant. (a) Estimate the feed rate of air to the Claus plant in \(\mathrm{kg} / \mathrm{kg}\) coal. (b) While the removal of sulfur emissions to the atmosphere is environmentally beneficial, identify an environmental concern that still must be addressed with the products from the Claus plant.

Short Answer

Expert verified
a) The feed rate of air to the Claus plant is 0.0402 kg air/kg coal. b) The management and disposal of elemental sulfur and other chemical wastes produced by the Claus process is an environmental concern.

Step by step solution

01

Determine Quantity of Sulfur

First, one must calculate the amount of sulfur in a one kg of coal. From the given data, it is known that coal consists of 0.6 wt\% sulfur. Hence, the quantity of sulfur in 1 kg of coal will be 0.006 kg.
02

Convert Sulfur to \(H_{2}S\)

The problem states that all sulfur is converted to \(H_{2}S\). So, calculate the number of moles. The molar mass of \(H_{2}S\) is approximately 34 g/mol or 0.034 kg/mol. Therefore, 0.006 kg of sulfur is equivalent to 0.006 kg/0.034 kg/mol = 0.176 moles of \(H_{2}S\).
03

Calculate Quantity of Oxygen Needed

The reaction is \(H_{2}S + \frac{3}{2}O_{2} \rightarrow SO_{2} + H_2O\). From the stoichiometry of the reaction, 1 mol of \(H_{2}S\) reacts with 1.5 mol of \(O_2\). Therefore, 0.176 moles of \(H_{2}S\) will require 0.176 * 1.5 = 0.264 moles of \(O_2\).
04

Convert Quantity of Oxygen to Mass

The molar mass of oxygen is 32 g/mol or 0.032 kg/mol. Therefore, 0.264 moles of \(O_2\) is equivalent to 0.264 * 0.032 = 0.00845 kg.
05

Calculate Air Feed Rate

Air consists of approximately 21 wt\% oxygen. Therefore, the mass of air needed to provide 0.00845 kg of oxygen is 0.00845/0.21 = 0.0402 kg. Hence, the feed rate of air to the Claus plant is 0.0402 kg air per kg of coal.
06

Identify an Environmental Concern

The Claus process produces waste that includes water and elemental sulfur as byproducts. Though sulfur is less harmful than its gaseous forms, the disposal and management of such chemical waste is an environmental concern.

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Key Concepts

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

Chemical Engineering and the Claus Process
Chemical engineering plays a crucial role in transforming raw materials into valuable products while addressing environmental concerns. One notable application is the Claus process, which is effectively harnessed to mitigate pollution by converting hazardous sulfur compounds into elemental sulfur. This catalytic chemical process, typically used in refineries and chemical plants, highlights the field's commitment to sustainability and public health.

The Claus process, in its operation, involves two main chemical reactions. Initially, a portion of hydrogen sulfide (\(H_2S\)) from the acid-gas is combusted with oxygen to form water (\(H_2O\)) and sulfur dioxide (\(SO_2\)). Subsequently, in a catalytic reactor, the remaining \(H_2S\) reacts with the produced \(SO_2\) to yield elemental sulfur. This dual-stage approach ensures that sulfur, a detrimental pollutant, is not released into the atmosphere but is instead captured as a solid. By tackling the problem of sulfur emissions, chemical engineers utilize the Claus process as a testament to their expertise in designing processes which are both efficient and environmentally considerate.
Environmental Impact of Gasification and Sulfur Recovery
The environmental impact of gasification processes, which convert carbonaceous materials into synthetic gas, cannot be overlooked. One critical aspect of gasification, particularly of coal, is the release of sulfur compounds such as \(H_{2}S\), which can lead to acid rain and respiratory problems. The integration of the Claus process in gasification plants showcases the industry's efforts in reducing the environmental footprint of such operations.

While the Claus process significantly diminishes the emission of sulfur into the atmosphere, an issue still persists with the handling of byproducts. The process generates a considerable amount of elemental sulfur, which must be managed responsibly to prevent environmental degradation. Thus, environmental engineers and chemical engineers must collaborate to develop robust strategies for sulfur waste disposal or repurposing, ensuring that the solutions implemented do not trade one environmental hazard for another.
Understanding Stoichiometry in the Claus Process
Stoichiometry, the cornerstone of chemical reactions, defines the proportional relationship between reactants and products. In the context of the Claus process, stoichiometry is pivotal to determining the precise quantities of reactants required for the efficient conversion of \(H_{2}S\) to sulfur.

In the exercise provided, we explore the stoichiometric calculations necessary for the Claus process to function. To find the air feed rate, one must determine the mass of sulfur in the coal, convert it to the equivalent mass of \(H_{2}S\), and then calculate the required oxygen. This meticulous approach, guided by stoichiometric principles, ensures the complete reaction of \(H_{2}S\) while minimizing excess reactants, which is fundamental for both economic and environmental optimality. Such exercises not only train students in computational skills but also instill an understanding of the precision required in chemical engineering practice.

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Most popular questions from this chapter

A liquid mixture containing ethanol ( 55.0 wt\%) and the balance water enters a separation process unit at a rate of \(90.5 \mathrm{kg} / \mathrm{s}\). A technician draws samples of the two product streams leaving the separator and analyzes them with a gas chromatograph, obtaining values of 86.2 wt\% ethanol (Product Stream 1) and \(10.9 \%\) ethanol (Product Stream 2). The technician then reads a manometer attached to an orifice meter mounted in the pipe carrying Product Stream 1, converts the reading to a volumetric flow rate using a calibration curve, and converts that result to a mass flow rate using the average density of ethanol and water. The result is \(54.0 \mathrm{kg} / \mathrm{s}\). Finally, the technician calculates the mass flow rate of the second product stream using a material balance and reports the calculated product stream flow rates and compositions to you. You examine them, do some calculations, and reject them. (a) Draw and label a flow chart of the separation process. (b) Carry out the calculations that led you to reject the submitted results and explain how you knew the values were wrong. (c) List up to five possible reasons for the incorrect results. For each one, briefly state how you might determine whether it was in fact a cause of error and what you might do to correct it if it was.

A fuel oil is analyzed and found to contain 85.0 wt\% carbon, \(12.0 \%\) elemental hydrogen (H), \(1.7 \%\) sulfur, and the remainder noncombustible matter. The oil is burned with \(20.0 \%\) excess air, based on complete combustion of the carbon to \(\mathrm{CO}_{2}\), the hydrogen to \(\mathrm{H}_{2} \mathrm{O}\), and the sulfur to \(\mathrm{SO}_{2}\). The oil is burned completely, but \(8 \%\) of the carbon forms CO. Calculate the molar composition of the stack gas.

A \(100 \mathrm{kmol} / \mathrm{h}\) stream that is 97 mole \(\%\) carbon tetrachloride \(\left(\mathrm{CCl}_{4}\right)\) and \(3 \%\) carbon disulfide \(\left(\mathrm{CS}_{2}\right)\) is to be recovered from the bottom of a distillation column. The feed to the column is 16 mole \(\% \mathrm{CS}_{2}\) and \(84 \% \mathrm{CCl}_{4},\) and \(2 \%\) of the \(\mathrm{CCl}_{4}\) entering the column is contained in the overhead stream leaving the top of the column. (a) Draw and label a flowchart of the process and do the degree-of-freedom analysis. (b) Calculate the mass and mole fractions of \(\mathrm{CCl}_{4}\) in the overhead stream, and determine the molar flow rates of \(\mathrm{CCl}_{4}\) and \(\mathrm{CS}_{2}\) in the overhead and feed streams. (c) Suppose the overhead stream is analyzed and the mole fraction of \(\mathrm{CS}_{2}\) is found to be significantly lower than the value calculated in Part (b). List as many reasons as you can for the discrepancy, including possible violations of assumptions made in Part (b).

In the Deacon process for the manufacture of chlorine, HCI and \(\mathrm{O}_{2}\) react to form \(\mathrm{Cl}_{2}\) and \(\mathrm{H}_{2} \mathrm{O}\) Sufficient air ( 21 mole \(\% \mathrm{O}_{2}, 79 \% \mathrm{N}_{2}\) ) is fed to provide \(35 \%\) excess oxygen, and the fractional conversion of HCl is \(85 \%\) (a) Calculate the mole fractions of the product stream components, using atomic species balances in your calculation. (b) Again calculate the mole fractions of the product stream components, only this time use the extent of reaction in the calculation. (c) An alternative to using air as the oxygen source would be to feed pure oxygen to the reactor. Running with oxygen imposes a significant extra process cost relative to running with air, but also offers the potential for considerable savings. Speculate on what the cost and savings might be. What would determine which way the process should be run?

\- An equimolar liquid mixture of benzene and toluene is separated into two product streams by distillation. A process flowchart and a somewhat oversimplified description of what happens in the process follow: Inside the column a liquid stream flows downward and a vapor stream rises. At each point in the column some of the liquid vaporizes and some of the vapor condenses. The vapor leaving the top of the column, which contains 97 mole\% benzene, is completely condensed and split into two equal fractions: one is taken off as the overhead product stream, and the other (the reflux) is recycled to the top of the column. The overhead product stream contains \(89.2 \%\) of the benzene fed to the column. The liquid leaving the bottom of the column is fed to a partial reboiler in which \(45 \%\) of it is vaporized. The vapor generated in the reboiler (the boilup) is recycled to become the rising vapor stream in the column, and the residual reboiler liquid is taken off as the bottom product stream. The compositions of the streams leaving the reboiler are governed by the relation $$\frac{y_{\mathrm{B}} /\left(1-y_{\mathrm{B}}\right)}{x_{\mathrm{B}} /\left(1-x_{\mathrm{B}}\right)}=2.25$$ where \(y_{\mathrm{B}}\) and \(x_{\mathrm{B}}\) are the mole fractions of benzene in the vapor and liquid streams, respectively. (a) Take a basis of 100 mol fed to the column. Draw and completely label a flowchart, and for each of four systems (overall process, column, condenser, and reboiler), do the degree-of-freedom analysis and identify a system with which the process analysis might appropriately begin (one with zero degrees of freedom). (b) Write in order the equations you would solve to determine all unknown variables on the flowchart, circling the variable for which you would solve in each equation. Do not do the calculations in this part. (c) Calculate the molar amounts of the overhead and bottoms products, the mole fraction of benzene in the bottoms product, and the percentage recovery of toluene in the bottoms product \((100 \times\) moles toluene in bottoms/mole toluene in feed).

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