/*! 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 39 The hormone estrogen is produced... [FREE SOLUTION] | 91Ó°ÊÓ

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The hormone estrogen is produced in the ovaries of females and elsewhere in the body in men and postmenopausal women, and it is also administered in estrogen replacement therapy, a common treatment for women who have undergone a hysterectomy. Unfortunately, it also binds to estrogen receptors in breast tissue and can activate cells to become cancerous. Tamoxifen is a drug that also binds to estrogen receptors but does not activate cells, in effect blocking the receptors from access to estrogen and inhibiting the growth of breast-cancer cells. Tamoxifen is administered in tablet form. In the manufacturing process, a finely ground powder contains tamoxifen (tam) and two inactive fillers- -lactose monohydrate (lac) and corn starch (cs). The powder is mixed with a second stream containing water and suspended solid particles of polyvinylpymolidone (pvp) binder, which keeps the tablets from easily crumbling. The slurry leaving the mixer goes to a dryer, in which 94.2\% of the water fed to the process is vaporized. The wet powder leaving the dryer contains 8.80 wr\% tam, 66.8\% lac, 21.4\% cs, 2.00\% pvp, and 1.00\% water. After some additional processing, the powder is molded into tablets. To produce a hundred thousand tablets, 17.13 kg of wet powder is required. (a) Taking a basis of 100,000 tablets produced, draw and label a process flowchart, labeling masses of individual components rather than total masses and component mass fractions. It is unnecessary to label the stream between the mixer and the dryer. Carry out a degree-of-freedom analysis of the overall two-unit process. (b) Calculate the masses and compositions of the streams that must enter the mixer to make 100,000 tablets. (c) Why was it unnecessary to label the stream between the mixer and the dryer? Under what circumstances would it have been necessary? (d) Go back to the flowchart of Part (a). Without using the mass of the wet powder (17.13 kg) or any of the results from Part (b) in your calculations, determine the mass fractions of the stream components in the powder fed to the mixer and verify that they match your solution to Part (b). (Hint: Take a basis of \(100 \mathrm{kg}\) of wet powder.) (e) Suppose a student does Part (d) before Part (b), and re-labels the powder feed to the mixer on the flowchart of Part (a) with an unknown total mass ( \(m_{1}\) ) and the three now known mole fractions. (Sketch the resulting flowchart.) The student then does a degree-of-freedom analysis, counts four unknowns (the masses of the powder, pvp, and water fed to the mixer, and the mass of water evaporated in the dryer), and six equations (five material balances for five species and the percentage evaporation), for a net of -2 degrees of freedom. since there are more equations than unknowns, it should not be possible to get a unique solution for the four unknowns. Nevertheless, the student writes four equations, solves for the four unknowns, and verifies that all of the balance equations are satisfied. There must have been a mistake in the degree-of-freedom calculation. What was it?

Short Answer

Expert verified
The process involves mixing tam, lac, cs with pvp and water. After the drying process where 94.2% of water is evaporated, the product is a wet powder that is then molded into tablets. The masses and compositions of streams entering the mixer are calculated by using material balances and the composition of the wet powder. The stream between the mixer and dryer does not need to be labeled because its mass does not affect the calculations. The mass fractions of the mixer feed are verified by taking a new basis. A student's degree-of-freedom analysis was incorrect due to miscounting the number of unknowns; the individual masses of the mixer components were actually dependent on the total mass of the powder feed, not independent.

Step by step solution

01

Drawing a Process Flowchart

First, draw a flowchart of the process: the tamoxifen (tam), lactose monohydrate (lac), and corn starch (cs) enter the mixer, get mixed with polyvinylpyrrolidone (pvp) and water, go through a dryer where 94.2% of the water is evaporated, and leaves the dryer as wet powder (containing 8.80% tam, 66.8% lac, 21.4% cs, 2.00% pvp, and 1.00% water) that is then processed into tablets.
02

Degree-of-freedom Analysis

For the degree-of-freedom analysis, first identify the number of unknowns and equations. In this case, there are five material balances (for tam, lac, cs, pvp, and water) and one additional equation from the percentage evaporation of water, making a total of six equations. The number of unknowns can be determined from the flowchart: each stream entering the mixer has an unknown mass, the mass of water evaporated is unknown, and the total mass of the exit stream from the mixer to the dryer is also unknown. This gives a total of four unknowns. Subtracting the number of equations from the number of unknowns (\(degrees\ of\ freedom = unknowns - equations\)) gives -2 degrees of freedom, meaning that the equations are overdetermined and there is no unique solution.
03

Calculation of the Masses and Compositions of Streams

To calculate the masses and compositions of the streams that enter the mixer to make 100,000 tablets, you need to use the material balances and the composition of the wet powder that leaves the dryer. First, calculate the mass of each component in the wet powder by multiplying the total mass of the wet powder used to produce 100,000 tablets (\(17.13\ kg\)) by the mass fraction of each component. Then, set up material balances for each component to solve for the masses of the components in the streams that enter the mixer. Note that for water, you have to account for the 94.2% that is evaporated in the dryer. The composition of each stream can then be calculated by dividing the mass of each component in a stream by the total mass of that stream.
04

Explanation for Unlabeled Stream

The stream between the mixer and the dryer was not labeled as its mass was not necessary for the calculations. It would have been necessary to label it and know its mass if the problem asked for the total mass balance around the mixer or the dryer, or if the water evaporation was not given as a percentage of the water fed to the process, but as a percentage of the mass of this stream.
05

Verification of Powder Feed to the Mixer

With a new basis of 100 kg of wet powder, calculate the mass of each component in the wet powder based on their mass fractions and then use the material balances as before to solve for the masses of the components in the stream entering the mixer. The mass fractions of the components in the stream entering the mixer are then calculated by dividing the mass of each component in this stream by the total mass of this stream. Compare these mass fractions with those obtained in Step 3 to verify that they are the same.
06

Analysis of Student's Mistake

Upon re-examining the degree-of-freedom analysis on the basis set by the student in step (e), it appears that the mistake lies in counting the degrees of freedom. While it's correct to count five material balances for five species and the percentage evaporation as six equations, the count of four unknowns is incorrect. The student didn't consider that once the mass fractions are known, the individual masses of the powder, pvp, and water fed to the mixer are not independent unknowns anymore, but are dependent on the unknown total mass of the powder feed to the mixer. Therefore, there are in fact only two independent unknowns in this case: the mass of the powder feed to the mixer and the mass of water evaporated in the dryer. This gives a total of four degrees of freedom (six equations - two unknowns= four), revealing that the student's calculation of -2 degrees of freedom was indeed an error.

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Key Concepts

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

Material Balances in Chemical Processes
Material balances are fundamental in chemical process analysis. These balances involve calculating the input, output, and accumulation of materials within a process. Understanding material balances allows engineers to determine the flow rates of all substances at various points in a system.

In the context of the tamoxifen tablet manufacturing process, material balances help track each ingredient, including tamoxifen, lactose monohydrate, corn starch, polyvinylpyrrolidone (pvp), and water. By knowing the amounts of these materials entering and leaving different sections of the process, engineers can maintain optimal production conditions and ensure the final formulation meets specifications.

**How to Apply a Material Balance:**
  • Identify each component that enters or leaves the system.
  • Set up an equation where the total inflow equals the total outflow for each component.
  • Use known mass fractions and total mass to calculate unknown quantities.
In the given exercise, such balances are crucial for determining the precise quantity of each raw material feeds into the mixer and the composition of the exiting product.
Degree-of-Freedom Analysis Explained
Degree-of-freedom analysis is an essential technique in chemical engineering used to determine how many properties or variables in a process can be independently set. It reveals whether a process is well-defined and if there are enough equations available to solve for the unknowns.

In the tamoxifen production problem, the degree-of-freedom analysis was used to assess the overall two-unit process involving mixing and drying. The analysis determined there were more equations than unknowns, leading to equations being overdetermined, which typically means a unique solution is not possible. However, this apparent contradiction occurred due to not correctly identifying the independent variables.

**Steps in Degree-of-Freedom Analysis:**
  • List all equations available for the system (material balances, additional relationships like percentage evaporation).
  • Count all unknowns in the process.
  • Calculate degrees of freedom by subtracting the number of equations from the number of unknowns.
  • If the result is zero, the problem may be theoretically solvable; a negative result suggests an error in the setup or analysis.
Accurate degree-of-freedom analysis is crucial for ensuring each variable in the process is appropriately accounted for and can be used effectively.
Estrogen, Tamoxifen, and Cancer Treatment
Estrogen plays a significant role in various bodily functions, but it can also be a double-edged sword by potentially triggering breast cancer cells. Tamoxifen is a widely used drug in cancer treatment because it binds to estrogen receptors without activating cancer cell proliferation.

This mode of action makes tamoxifen an effective agent in inhibiting the growth of estrogen-receptor-positive breast-cancer cells. It essentially competes with estrogen, blocking its access and thereby reducing the risk of cancer progression. Such treatments are critical for patients who are particularly vulnerable to estrogen-fueled cancers, including those undergoing estrogen replacement therapy post-hysterectomy.

Understanding this balance between beneficial hormone functions and potential cancer activation is vital for developing successful treatment strategies.
Principles of Flowchart Design
Flowchart design in chemical engineering visually represents processes to help understand and optimize them. A well-designed flowchart simplifies complex data and illustrates the pathway of materials and energy through the system.

For instance, in designing a flowchart for the tamoxifen production process, the crucial components like mixers, dryers, and streams of materials (like tamoxifen, fillers, and binders) are clearly detailed. Key information, such as mass fractions and compositions, can be annotated on the flowchart to provide a clear snapshot of what is happening in the process.

**Best Practices for Effective Flowchart Design:**
  • Clearly label all streams and components.
  • Indicate directions of material flow accurately.
  • Use consistent symbols for units and equipment to avoid confusion.
  • Provide necessary detail to allow for easy understanding without overcrowding for clarity.
By adhering to these principles, engineers can use flowcharts to diagnose process issues, facilitate communication among teams, and ultimately enhance process efficiency.

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Most popular questions from this chapter

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?)

A drug (D) is produced in a three-stage extraction from the leaves of a tropical plant. About 1000 kg of leaf is required to produce 1 kg of the drug. The extraction solvent (S) is a mixture containing 16.5 wt\% ethanol (E) and the balance water (W). The following process is carried out to extract the drug and recover the solvent. 1\. A mixing tank is charged with \(3300 \mathrm{kg}\) of \(\mathrm{S}\) and \(620 \mathrm{kg}\) of leaf. The mixer contents are stirred for several hours, during which a portion of the drug contained in the leaf goes into solution. The contents of the mixer are then discharged through a filter. The liquid filtrate, which carries over roughly \(1 \%\) of the leaf fed to the mixer, is pumped to a holding tank, and the solid cake (spent leaf and entrained liquid) is sent to a second mixer. The entrained liquid has the same composition as the filtrate and a mass equal to \(15 \%\) of the mass of liquid charged to the mixer. The extracted drug has a negligible effect on the total mass and volume of the spent leaf and the filtrate. 2\. The second mixer is charged with the spent leaf from the first mixer and with the filtrate from the previous batch in the third mixer. The leaf is extracted for several more hours, and the contents of the mixer are then discharged to a second filter. The filtrate, which contains \(1 \%\) of the leaf fed to the second mixer, is pumped to the same holding tank that received the filtrate from the first mixer, and the solid cake- -spent leaf and entrained liquid - is sent to the third mixer. The entrained liquid mass is \(15 \%\) of the mass of liquid charged to the second mixer. 3\. The third mixer is charged with the spent leaf from the second mixer and with \(2720 \mathrm{kg}\) of solvent \(\mathrm{S}\). The mixer contents are filtered; the filtrate, which contains \(1 \%\) of the leaf fed to the third mixer, is recycled to the second mixer; and the solid cake is discarded. As before, the mass of the entrained liquid in the solid cake is \(15 \%\) of the mass of liquid charged to the mixer. 4\. The contents of the filtrate holding tank are filtered to remove the carried-over spent leaf, and the wet cake is pressed to recover entrained liquid, which is combined with the filtrate. A negligible amount of liquid remains in the wet cake. The filtrate, which contains \(\mathrm{D}, \mathrm{E},\) and \(\mathrm{W},\) is pumped to an extraction unit (another mixer). 5\. In the extraction unit, the alcohol-water-drug solution is contacted with another solvent (F), which is almost but not completely immiscible with ethanol and water. Essentially all of the drug (D) is extracted into the second solvent, from which it is eventually separated by a process of no concern in this problem. Some ethanol but no water is also contained in the extract. The solution from which the drug has been extracted (the raffinate) contains \(13.0 \mathrm{wt} \% \mathrm{E}, 1.5 \% \mathrm{F},\) and \(85.5 \%\) W. It is fed to a stripping column for recovery of the ethanol. 6\. The feeds to the stripping column are the solution just described and steam. The two streams are fed in a ratio such that the overhead product stream from the column contains \(20.0 \mathrm{wt} \% \mathrm{E}\) and \(2.6 \% \mathrm{F},\) and the bottom product stream contains \(1.3 \mathrm{wt} \% \mathrm{E}\) and the balance \(\mathrm{W}\). Draw and label a flowchart of the process, taking as a basis one batch of leaf processed. Then calculate (a) the masses of the components of the filtrate holding tank. (b) the masses of the components \(D\) and \(E\) in the extract stream leaving the extraction unit. (c) the mass of steam fed to the stripping column, and the masses of the column overhead and bottoms products.

A liquid mixture contains \(60.0 \mathrm{wt} \%\) ethanol \((\mathrm{E}), 5.0 \mathrm{wt} \%\) of a dissolved solute \((\mathrm{S}),\) and the balance water. A stream of this mixture is fed to a continuous distillation column operating at steady state. Product streams emerge at the top and bottom of the column. The column design calls for the product streams to have equal mass flow rates and for the top stream to contain 90.0 wt\% ethanol and no S. (a) Assume a basis of calculation, draw and fully label a process flowchart, do the degree-of-freedom analysis, and verify that all unknown stream flows and compositions can be calculated. (Don't do any calculations yet.) (b) Calculate (i) the mass fraction of \(S\) in the bottom stream and (ii) the fraction of the ethanol in the feed that leaves in the bottom product stream (i.e., \(\mathrm{kg} \mathrm{E}\) in bottom stream/kg \(\mathrm{E}\) in feed) if the process operates as designed. (c) An analyzer is available to determine the composition of ethanol-water mixtures. The calibration curve for the analyzer is a straight line on a plot on logarithmic axes of mass fraction of ethanol, \(x\) (kg E/kg mixture), versus analyzer reading, \(R\). The line passes through the points \((R=15, x=\) 0.100) and \((R=38, x=0.400)\). Derive an expression for \(x\) as a function of \(R(x=\cdots\) ) based on the calibration, and use it to determine the value of \(R\) that should be obtained if the top product stream from the distillation column is analyzed. (d) Suppose a sample of the top stream is taken and analyzed and the reading obtained is not the one calculated in Part (c). Assume that the calculation in Part (c) is correct and that the plant operator followed the correct procedure in doing the analysis. Give five significantly different possible causes for the deviation between \(R_{\text {measured and }} R_{\text {prediced }}\), including several assumptions made when writing the balances of Part (c). For each one, suggest something that the operator could do to check whether it is in fact the problem.

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.

Liquid methanol is fed to a space heater at a rate of \(12.0 \mathrm{L} / \mathrm{h}\) and burned with excess air. The product gas is analyzed and the following dry-basis mole percentages are determined: \(\mathrm{CH}_{3} \mathrm{OH}=0.45 \%\) \(\mathrm{CO}_{2}=9.03 \%,\) and \(\mathrm{CO}=1.81 \%\) (a) Draw and label a flowchart and verify that the system has zero degrees of freedom. (b) Calculate the fractional conversion of methanol, the percentage excess air fed, and the mole fraction of water in the product gas. (c) Suppose the combustion products are released directly into a room. What potential problems do you see and what remedies can you suggest?

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