/*! 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 59 The current global reliance on f... [FREE SOLUTION] | 91Ó°ÊÓ

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The current global reliance on fossil fuels for heating, transportation, and electric power generation raises concems regarding the release of \(\mathrm{CO}_{2}\) and \(\mathrm{CH}_{4},\) which are greenhouse gases thought to lead to climate change, and NO, which contributes to smog. One potential solution to these problems is to produce transportation fuels from renewable biomass. You have been asked to evaluate a proposed process for converting forest residues to alcohols that may be used as transportation fuels. In the first stage of the process, steam and dry wood from hybrid poplar trees (which grow between five and eight feet a year and can be harvested roughly every five years) are fed to a gasifier in which the biomass is converted to light gases in the following reactions: $$\begin{aligned} \mathrm{C}+\mathrm{H}_{2} \mathrm{O} & \rightarrow \mathrm{CO}+\mathrm{H}_{2} \\\ \mathrm{CO}+\mathrm{H}_{2} \mathrm{O} & \rightarrow \mathrm{CO}_{2}+\mathrm{H}_{2} \\ \mathrm{C}+\mathrm{CO}_{2} & \rightarrow 2 \mathrm{CO} \\ \mathrm{C}+2 \mathrm{H}_{2} & \rightarrow \mathrm{CH}_{4} \\ \mathrm{CH}_{4}+\mathrm{H}_{2} \mathrm{O} & \rightarrow \mathrm{CO}+3 \mathrm{H}_{2} \end{aligned}$$ The effluents from the reactor are a gas stream containing \(\mathrm{H}_{2}, \mathrm{CO}, \mathrm{CO}_{2}, \mathrm{CH}_{4},\) and \(\mathrm{H}_{2} \mathrm{O},\) and a solid char stream that contains only carbon and hydrogen. The char is discarded and the gases go through additional steps in which the hydrogen and carbon monoxide are converted to mixed alcohols. This problem only concerns the gasifier. \(\cdot\) Elemental composition of biomass: 51.9 mass \(\%\) C \(, 6.3 \%\) H, and \(41.8 \%\) O \(\cdot\) Pressure and temperature of entering steam: \(155^{\circ} \mathrm{C}, 4.4 \mathrm{atm}\) \(\cdot\) Feed ratio of steam to biomass: 1.1 kg steam/kg biomass \(\cdot\) Yield and dry-basis composition of product gas: 1.35 kg dry gas/kg biomass at \(700^{\circ} \mathrm{C}, 1.2\) atm; 50.7 mol\% \(\mathrm{H}_{2}, 23.8 \%\) CO, \(18.0 \% \mathrm{CO}_{2}, 7.5 \% \mathrm{CH}_{4}\) (a) Taking a basis of \(100 \mathrm{kg}\) of biomass fed, draw and completely label a flowchart for the gasifier incorporating the given data, labeling the volumes of the steam fed and the gases produced. Perform a degree-of-freedom analysis. (b) Calculate the mass and mass composition of the char and the volumes of the steam feed and product gas streams. (c) List advantages and possible drawbacks of using biomass rather than petroleum as a fuel source.

Short Answer

Expert verified
Flowchart: This can be drawn with the given inputs and outputs for the gasifier, showing the feed of biomass and steam and the production of gases as outputs along with char. Degree of freedom analysis: -1, suggesting that additional information (which is given) is needed to fully define the system.Mass of steam feed: 110 kg. Mass of char: The difference between the initial biomass mass and the mass of steam and gases produced.Volumes of feeds and products: These can be estimated using the ideal gas law and information given on pressures, temperatures and compositions. Biomass usage: The pros and cons are closely tied to the environmental and economical impacts, with advantages including its renewability and lower emissions, and disadvantages which could involve its implications for land and water resources, and processing technology requirements.

Step by step solution

01

- Creating a flowchart and Performing a degree of freedom analysis

One can create a flowchart quite simply by starting at the beginning of the process (the introduction of dry wood and steam) and following the process through to the end (the output of a gas stream and solid char). Remember to incorporate the given data.Perform a degree-of-freedom analysis using the formula:\[DOF = c - s - p + 1\]where \(c\) is the number of components, \(s\) is the number of species and \(p\) is the number of phases present.In this case: \(c = 4\) (H2, CO, CO2 and CH4), \(s = 5\) (H2, CO, CO2, CH4 and H2O) and \(p = 1\)So, \[DOF = 4 - 5 - 1 + 1 = -1\]This suggests that there is one unknown too many and thus additional information would be required to solve this problem. In this case, the 'additional' information is given as the product gas composition.
02

- Calculating mass and composition of the char and volumes of steam feed and product gas streams

The mass of biomass feed is given as 100 kg, with mass composition of 51.9 % C, 6.3 % H, and 41.8 % O by mass. The overall feed also contains steam and the mass ratio of steam to biomass is given as 1.1. Thus, the mass of steam equals 1.1 x 100 kg = 110 kg.Based on the given yield, 1.35 kg dry gas is produced per kg biomass, so for 100 kg biomass, it would be 1.35 x 100 = 135 kg dry gas. The remaining mass would be the char as the gases produced are known.The volumes of the steam and gas streams can be approximated using the ideal gas law together with the conditions of pressure and temperature given, with the molar fraction of each component, but taking into account that the volume is not necessarily additive.
03

- Listing advantages and drawbacks of using biomass.

Advantages of using biomass instead of petroleum as a fuel source can include: its renewability, reduced greenhouse gas emissions (as the CO2 released is offset by the CO2 absorbed during the growth of the biomass), and its potential to cause less damage to the environment in the event of a spill. Potential drawbacks could include: the requirement of land and resources for growing biomass, possible interference with food production, possible increase in water usage, and the need for complex and potentially costly technologies for processing and conversion.

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Key Concepts

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

Chemical Process Design
Understanding Chemical Process Design is pivotal when considering the transformation of renewable resources, like biomass, into fuel. The process involves the strategic conversion of raw materials—such as dry wood from trees—into more valuable products using chemical reactions. This transformation is managed within a chemical reactor, here, a biomass gasifier.
When designing such a chemical process, considerations include reaction stoichiometry, energy balances, and material flows. Efficiency, safety, and environmental impact are also significant concerns due to the greenhouse gases involved. In the context of the given exercise, the design must efficiently convert the biomass to gas while minimizing the output of harmful substances.
To improve understanding, visual aids like flowcharts and step-by-step exercises enable students to methodically follow the complex process.
Flowchart Creation
Creating a Flowchart is a fundamental step in visualizing the sequence and interaction of events in a chemical process. Flowcharts provide a bird's-eye view of the entire process, showcasing each step from the initial inputs to the final outputs.
For the biomass gasifier process, it's key to construct a clear diagram detailing the inputs (steam and dry wood), the chemical reactions, and the outputs (gas stream and solid char). Labeling each element, such as flow rates, stream composition, and operating conditions, can make the system easier to analyze and understand. This visual representation helps in identifying process relationships and systems, essential in enabling students to recognize the significance of each step in the conversion of biomass to fuel.
Degree-of-Freedom Analysis
Degree-of-Freedom Analysis is a quantitative tool employed to ascertain if the available information about a process is sufficient to calculate unknowns. It's essentially a count of variables versus equations available. The term 'degree-of-freedom' refers to the number of independent variables that can be changed without affecting others.
In chemical process calculation, it's determined by the formula \[DOF = c - s - p + 1\]. This concept alerts you to either an excess or deficit of information required to solve a problem. In the gasifier scenario, the analysis revealed an additional piece of data needed, pointing to the necessity of product gas composition for fully determining outputs. This analytical approach is crucial in troubleshooting and ensuring the completeness of information in process design.
Gas Stream Composition Analysis
Gas Stream Composition Analysis is vital in assessing the efficiency and quality of the chemical processes. In the case of the gasifier, it entails examining the mixture of gases produced—hydrogen (\(H_2\)), carbon monoxide (\(CO\)), carbon dioxide (\(CO_2\)), and methane (\(CH_4\)). Knowing the molar or mass percentage composition of these gases is critical for optimizing the performance of the subsequent alcohol synthesis process and for environmental compliance.
Analysis of gas stream composition aids in determining if the reaction has proceeded as intended or if adjustments in process conditions or feedstocks are necessary. For students, understanding how to perform such an analysis can shape the way they approach problems requiring accuracy of composition for successful outcomes.
Renewable Energy Sources
Considering Renewable Energy Sources is imperative due to the burdensome environmental and economic impacts of fossil fuels. Biomass, as showcased in the exercise, represents a renewable source that can potentially lead to the production of cleaner fuels. Unlike fossil fuels, biomass can be replenished quickly and continuously, aligning with sustainable practices.
While biomass offers benefits like reducing greenhouse gas emissions, the process of converting biomass to fuel requires careful evaluation of its own environmental impacts, such as land use and water consumption. For students learning about renewable energy, understanding the characteristics, benefits, and drawbacks of various sources, including biomass, provides a comprehensive view of existing and future energy solutions.

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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 gas cylinder filled with nitrogen at standard temperature and pressure has a mass of \(37.289 \mathrm{g}\). The same container filled with carbon dioxide at STP has a mass of 37.440 g. When filled with an unknown gas at STP, the container mass is \(37.062 \mathrm{g}\). Calculate the molecular weight of the unknown gas, and then state its probable identity.

Magnesium sulfate has a number of uses, some of which are related to the ability of the anhydrate form to remove water from air and others based on the high solubility of the heptahydrate \(\left(\mathrm{MgSO}_{4} \cdot 7 \mathrm{H}_{2} \mathrm{O}\right)\) form, also known as Epsom salt. The densities of the anhydrate and heptahydrate crystalline forms are 2.66 and \(1.68 \mathrm{g} / \mathrm{mL},\) respectively. Suppose you wish to form a 20.0 wt\% \(\mathrm{MgSO}_{4}\) aqueous solution by simply pouring crystals of one of the forms into a tank of water while the temperature is held constant at \(30^{\circ} \mathrm{C}\). The specific gravity of the 20.0 wt\% solution at \(30^{\circ} \mathrm{C}\) is \(1.22 .\) Answer the following questions for both forms of the \(\mathrm{MgSO}_{4}\) crystals: (a) What volume of water should be in the tank before crystals are added if the final product is to be 1000 kg of the 20 wt\% solution? (b) Suppose the tank diameter is \(0.30 \mathrm{m}\). What is the height of liquid in the tank before the crystals are added? (c) What is the height of the water in the tank after addition of the crystals but before they begin to dissolve? (d) What is the height of liquid in the tank after all the MgSO \(_{4}\) has dissolved?

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?

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.

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