/*! 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 58 Carbon nanotubes (CNT) are among... [FREE SOLUTION] | 91Ó°ÊÓ

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Carbon nanotubes (CNT) are among the most versatile building blocks in nanotechnology. These unique pure carbon materials resemble rolled-up sheets of graphite with diameters of several nanometers and lengths up to several micrometers. They are stronger than steel, have higher thermal conductivities than most known materials, and have electrical conductivities like that of copper but with higher currentcarrying capacity. Molecular transistors and biosensors are among their many applications. While most carbon nanotube research has been based on laboratory-scale synthesis, commercial applications involve large industrial-scale processes. In one such process, carbon monoxide saturated with an organo-metallic compound (iron penta-carbonyl) is decomposed at high temperature and pressure to form CNT, amorphous carbon, and CO_. Each "molecule" of CNT contains roughly 3000 carbon atoms. The reactions by which such molecules are formed are: In the process to be analyzed, a fresh feed of CO saturated with \(\mathrm{Fe}(\mathrm{CO})_{5}(\mathrm{v})\) contains \(19.2 \mathrm{wt} \%\) of the latter component. The feed is joined by a recycle stream of pure CO and fed to the reactor, where all of the iron penta-carbonyl decomposes. Based on laboratory data, \(20.0 \%\) of the CO fed to the reactor is converted, and the selectivity of CNT to amorphous carbon production is (9.00 kmol CNT/kmol C). The reactor effluent passes through a complex separation process that yields three product streams: one consists of solid \(\mathrm{CNT}, \mathrm{C},\) and \(\mathrm{Fe} ;\) a second is \(\mathrm{CO}_{2} ;\) and the third is the recycled \(\mathrm{CO}\). You wish to determine the flow rate of the fresh feed (SCM/h), the total CO_ generated in the process ( \(\mathrm{kg} / \mathrm{h}\) ), and the ratio (kmol CO recycled/kmol CO in fresh feed). (a) Take a basis of \(100 \mathrm{kmol}\) fresh feed. Draw and fully label a process flow chart and do degree-offreedom analyses for the overall process, the fresh-feed/recycle mixing point, the reactor, and the separation process. Base the analyses for reactive systems on atomic balances. (b) Write and solve overall balances, and then scale the process to calculate the flow rate (SCM/h) of fresh feed required to produce \(1000 \mathrm{kg} \mathrm{CNT} / \mathrm{h}\) and the mass flow rate of \(\mathrm{CO}_{2}\) that would be produced. (c) In your degree-of-freedom analysis of the reactor, you might have counted separate balances for C (atomic carbon) and O (atomic oxygen). In fact, those two balances are not independent, so one but not both of them should be counted. Revise your analysis if necessary, and then calculate the ratio (kmol CO recycled/kmol CO in fresh feed). (d) Prove that the atomic carbon and oxygen balances on the reactor are not independent equations.

Short Answer

Expert verified
The problem involves analyzing a process of synthesizing Carbon NanoTubes (CNT) from CO and \(\mathrm{Fe}(\mathrm{CO})_{5}\), drawing the relevant process flow, performing atomic and overall balances, and degree-of-freedom analyses. The process is also scaled up to determine the flow rate of CO_2 produced when 1000 kg/h of CNT is required. Additionally, it was shown that atomic carbon and oxygen balances are not independent in this case.

Step by step solution

01

Comprehensive Process Understanding

The problem involves the conversion of carbon monoxide (CO) and iron penta-carbonyl (\(\mathrm{Fe}(\mathrm{CO})_{5}\)) into carbon nanotubes (CNT), amorphous carbon (C), and iron (Fe). The basic understanding of this process is essential, including the feed constituents, conversion process, product streams, and effluents.
02

Drawing and Labelling the Process Flow Chart

A process flow diagram is to be created illustrating the CO and \(\mathrm{Fe}(\mathrm{CO})_{5}\) input, the reactor where the reaction takes place, the separation process, and the output streams which include CNT, C, CO_2 and recycled CO. Don't forget to mention the percent conversion, selectivity, and weight fractions where applicable.
03

Degree-of-Freedom Analysis

The degree of freedom is determined for the overall process, the fresh-feed/recycle mixing point, the reactor, and the separation process. This analysis involves determining the number of unknowns, the available balances and other equations, and subtracting the latter from the former.
04

Applying Material Balances

Material balances for carbon, oxygen, and iron in the reactor and overall process are written based on the reaction stoichiometry. For instance, carbon balance implies that the carbon entering the reactor with CO and \(\mathrm{Fe}(\mathrm{CO})_{5}\) equals the carbon leaving with CNT and CO_2, which can be written as \(CO_{in} + CNT_{out} = CO_{out} + \mathrm{Fe}(\mathrm{CO})_{5-in}\). Solution for these equations yields the flow rates of product and effluent streams.
05

Scaling up process

Using the results from the balance equations and given information, the process is scaled up to determine the flow rate of CO_2 produced when 1000 kg/h of CNT is required. This would demand proportional increase in the fresh feed flow rate as well.
06

Analysing Reactor's Degree of Freedom

The degree of freedom for the reactor is reanalyzed considering that the atomic carbon and oxygen balances are not independent (as the oxygen comes solely from the decomposition of CO). Therefore, only one of these balances should be included in the degree-of-freedom calculation.
07

Deriving Ratio of Recycled CO to CO in fresh feed

With the revised degree of freedom analysis, further calculation can be done to derive kmol CO recycled/kmol CO in fresh feed by using the balanced equations provided in step 4.
08

Independent Equation Analysis

An independent equation requires unique information that isn't represented in any other equation. To prove that atomic carbon and oxygen are not independent equations, it is enough to show that the information in the oxygen balance can be obtained from the carbon balance and vice versa, making them dependent. Hence, only one of them should be counted in the degree-of-freedom analysis.

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Key Concepts

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

Carbon Nanotubes
Carbon nanotubes (CNTs) represent a fascinating advancement in nanotechnology. Imagine sheets of graphite, intricately rolled into tiny tubes with diameters as narrow as a few nanometers and lengths extending to several micrometers. This unique structure gives CNTs extraordinary properties: they are exceptionally strong, exhibiting strength greater than steel. Their thermal conductivity surpasses many known materials, while their electrical conductivity rivals that of copper. This combination of properties makes them ideal for numerous applications like molecular transistors and biosensors.

However, producing CNTs on a commercial scale means moving from lab-bench experiments to large industrial processes. In these processes, specific reactions involve carbon monoxide and iron penta-carbonyl to produce not only CNTs but other forms of carbon, including amorphous carbon. Understanding these reactions and how CNTs form is key to efficiently designing processes that maximize CNT output while minimizing byproducts. As such, expertise in CNT production is critical for the development of new and existing technologies.
Process Flow Chart
Creating a process flow chart is like drafting a map of how substances move through a chemical process. It visually represents what enters and exits a process, as well as the pathways they take. For the case of carbon nanotube production, a flow chart would start with inputs such as carbon monoxide and iron penta-carbonyl, and track their transformation through a reactor.

This chart would include:
  • The reactor, where these compounds undergo decomposition.
  • The separation system, sorting solid CNTs and carbon from gases like carbon dioxide and remaining carbon monoxide.
  • Streams showing recycled and purged components.
Each part of the process must be labeled with pertinent information, such as feed rates, conversion percentages, and any material that gets recycled. A well-drafted flow chart aids engineers in understanding process efficiencies and where to apply improvements.

Through a comprehensive diagram, processes become more straightforward to manage, simplifying the complexity found in industrial-scale CNT production.
Material Balances
Material balances are fundamental to chemical engineering and ensure that all material entering a system is accounted for within the system and in the output. In the scenario of carbon nanotube synthesis, material balances involve tracking each atom or molecule through the process.

Key steps include:
  • Counting the carbon from CO and \( ext{Fe(CO)}_5 \) in the feed and comparing it to the carbon in CNTs and carbon dioxide in the products.
  • Assessing any byproducts, like amorphous carbon, and ensuring they match with the starting material.
This translates into equations derived from the stoichiometry of the reactions. For example, a material balance might be expressed as \( CO_{\text{in}} + CNT_{\text{out}} = CO_{\text{out}} + \left( ext{Fe(CO)}_5 \right)_{\text{in}} \). Solutions to these equations inform engineers of flow rates and compositions of various streams.

Proper material balancing ensures process efficiency and supports decision-making in design and operation.
Degree of Freedom Analysis
Degree of freedom analysis is a crucial tool in chemical process engineering that determines how many variables you can adjust independently without altering the system's equilibrium. It involves comparing the number of unknowns with the number of available equations. For a reactor where CNTs are produced, degree of freedom analysis ensures that the given process information is sufficient to solve for the unknowns.

Here's how you do it:
  • Identify all variables, such as flow rates or compositions of the inputs and outputs.
  • Write down all the balances, particularly for elements like carbon and oxygen.
  • Count the number of independent equations you have.
In this particular case, it's essential to recognize that not all balances (such as carbon and oxygen) are independent. The oxygen balance stems from a single source, complicating initial calculations. By re-evaluating which equations are dependent or redundant, one can accurately compute variables like the ratio of recycled CO to fresh feed CO.

Conducting a thorough degree of freedom analysis enhances our understanding of complex processes, ensuring more accurate design and optimization.

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Most popular questions from this chapter

In the production of soybean oil, dried and flaked soybeans are brought into contact with a solvent (often hexane) that extracts the oil and leaves behind the residual solids and a small amount of oil. (a) Draw a flowchart of the process, labeling the two feed streams (beans and solvent) and the leaving streams (solids and extract). (b) The soybeans contain 18.5 wt\% oil and the remainder insoluble solids, and the hexane is fed at a rate corresponding to \(2.0 \mathrm{kg}\) hexane per \(\mathrm{kg}\) beans. The residual solids leaving the extraction unit contain 35.0 wt\% hexane, all of the non-oil solids that entered with the beans, and \(1.0 \%\) of the oil that entered with the beans. For a feed rate of \(1000 \mathrm{kg} / \mathrm{h}\) of dried flaked soybeans, calculate the mass flow rates of the extract and residual solids, and the composition of the extract. (c) The product soybean oil must now be separated from the extract. Sketch a flowchart with two units, the extraction unit from Parts (a) and (b) and the unit separating soybean oil from hexane. Propose a use for the recovered hexane.

A stream of humid air containing 1.50 mole \(\% \mathrm{H}_{2} \mathrm{O}(\mathrm{v})\) and the balance dry air is to be humidified to a water content of 10.0 mole\% \(\mathrm{H}_{2} \mathrm{O}\). For this purpose, liquid water is fed through a flowmeter and evaporated into the air stream. The flowmeter reading, \(R\), is \(95 .\) The only available calibration data for the flowmeter are two points scribbled on a sheet of paper, indicating that readings \(R=15\) and \(R=50\) correspond to flow rates \(\dot{V}=40.0 \mathrm{ft}^{3} / \mathrm{h}\) and \(\dot{V}=96.9 \mathrm{ft}^{3} / \mathrm{h},\) respectively. (a) Assuming that the process is working as intended, draw and label the flowchart, do the degree-offreedom analysis, and estimate the molar flow rate (lb-mole/h) of the humidified (outlet) air if (i) the volumetric flow rate is a linear function of \(R\) and (ii) the reading \(R\) is a linear function of \(\dot{V}^{0.5}\) (b) Suppose the outlet air is analyzed and found to contain only \(7 \%\) water instead of the desired \(10 \%\) List as many possible reasons as you can think of for the discrepancy, concentrating on assumptions made in the calculation of Part (a) that might be violated in the real process.

A paint mixture containing \(25.0 \%\) of a pigment and the balance binders (which help the pigment stick to the surface) and solvents (which ensure that the paint stays in liquid form) sells for 18.00 dollar/kg, and a mixture containing 12.0\% sells for 10.00 dollar /kg. (a) If a paint retailer produces a blend containing \(17.0 \%\) pigment, for how much (S/kg) should it be sold to yield a 10\% profit? (b) Paint manufacturers have begun to market "low VOC" paint as a more environmentally friendly product. What are VOCs? List some ways in which paint products can be altered to lower the VOC content.

Methanol is produced by reacting carbon monoxide and hydrogen. A fresh feed stream containing \(\mathrm{CO}\) and \(\mathrm{H}_{2}\) joins a recycle stream and the combined stream is fed to a reactor. The reactor outlet stream flows at a rate of \(350 \mathrm{mol} / \mathrm{min}\) and contains \(10.6 \mathrm{wt} \% \mathrm{H}_{2}, 64.0 \mathrm{wt} \% \mathrm{CO},\) and \(25.4 \mathrm{wt} \% \mathrm{CH}_{3} \mathrm{OH} .\) (Notice that those are percentages by mass, not mole percents.) This stream enters a cooler in which most of the methanol is condensed. The liquid methanol condensate is withdrawn as a product, and the gas stream leaving the condenser- -which contains \(\mathrm{CO}, \mathrm{H}_{2},\) and \(0.40 \mathrm{mole} \%\) uncondensed \(\mathrm{CH}_{3} \mathrm{OH}\) vapor \(-\mathrm{is}\) the recycle stream that combines with the fresh feed. (a) Without doing any calculations, prove that you have enough information to determine (i) the molar flow rates of CO and \(\mathrm{H}_{2}\) in the fresh feed, (ii) the production rate of liquid methanol, and (iii) the single-pass and overall conversions of carbon monoxide. Then perform the calculations. (b) After several months of operation, the flow rate of liquid methanol leaving the condenser begins to decrease. List at least three possible explanations of this behavior and state how you might check the validity of each one. (What would you measure and what would you expect to find if the explanation is valid?)

L-Serine is an amino acid that often is provided when intravenous feeding solutions are used to maintain the health of a patient. It has a molecular weight of \(105,\) is produced by fermentation and recovered and purified by crystallization at \(10^{\circ} \mathrm{C}\). Yield is enhanced by adding methanol to the system, thereby reducing serine solubility in aqueous solutions. An aqueous serine solution containing 30 wt\% serine and \(70 \%\) water is added along with methanol to a batch crystallizer that is allowed to equilibrate at \(10^{\circ} \mathrm{C}\). The resulting crystals are recovered by filtration; liquid passing through the filter is known as filtrate, and the recovered crystals may be assumed in this problem to be free of adhering filtrate. The crystals contain a mole of water for every mole of serine and are known as a monohydrate. The crystal mass recovered in a particular laboratory run is \(500 \mathrm{g},\) and the filtrate is determined to be \(2.4 \mathrm{wt} \%\) serine, \(48.8 \%\) water, and \(48.8 \%\) methanol. (a) Draw and label a flowchart for the operation and carry out a degree-of- freedom analysis. Determine the ratio of mass of methanol added per unit mass of feed. (b) The laboratory process is to be scaled to produce \(750 \mathrm{kg} / \mathrm{h}\) of product crystals. Determine the required aqueous serine solution rates of aqueous serine solution and methanol.

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