/*! 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 46 Mammalian cells can be cultured ... [FREE SOLUTION] | 91Ó°ÊÓ

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Mammalian cells can be cultured for a variety of purposes, including synthesis of vaccines. They must be maintained in growth media containing all of the components required for proper cellular function to ensure their survival and propagation. Traditionally, growth media were prepared by blending a powder, such as Dulbecco's Modified Eagle Medium (DMEM) with sterile deionized water. DMEM contains glucose, buffering agents, proteins, and amino acids. Using a sterile (i.e., bacterial-, fungal-,and yeast-free) growth medium ensures proper cell growth, but sometimes the water (or powder) can become contaminated, requiring the addition of antibiotics to eliminate undesired contaminants. The culture medium is supplemented with fetal bovine serum (FBS) that contains additional growth factors required by the cells. Suppose an aqueous stream (SG = 0.90) contaminated with bacteria is split, with 75\% being fed to a mixing unit to dissolve a powdered mixture of DMEM contaminated with the same bacteria found in the water. The ratio of impure feed water to powder entering the mixer is 4.4:1. The stream leaving the mixer (containing DMEM, water, and bacteria) is combined with the remaining 25\% of the aqueous stream and fed to a filtration unit to remove all of the bacteria that have contaminated the system, a total of \(20.0 \mathrm{kg}\). Once the bacteria have been removed, the sterile medium is combined with FBS and the antibiotic cocktail PSG (Penicillin-Streptomycin-L-Glutamine) in a shaking unit to generate 5000 L of growth medium (SG = 1.2). The final composition of the growth medium is 66.0 wt\% H_O, 11.0\% FBS, 8.0\% PSG, and the balance DMEM. (a) Draw and label the process flowchart. (b) Do a degree-of-freedom analysis around each piece of equipment (mixer, filter, and shaker), the splitter, the mixing point, and the overall system. Based on the analysis, identify which system or piece of equipment should be the starting point for further calculations. (c) Calculate all of the unknown process variables. (d) Determine a value for (i) the mass ratio of sterile growth medium product to feed water and (ii) the mass ratio of bacteria in the water to bacteria in the powder. (e) Suggest two reasons why the bacteria should be removed from the system.

Short Answer

Expert verified
The processed growth medium will be purely composed of water, FBS, PSG, and DMEM devoid of any bacterial content. The mass ratio of sterile growth medium to feed water, and the mass ratio of bacteria in the water to bacteria in the powder, can be calculated using mass balance principles. Bacteria removal is crucial to keep the medium sterile and to prevent negative effects on the cells.

Step by step solution

01

Drawing and labeling the process flowchart

Start by choosing symbols to represent the components involved in the process, such as a line for connecting elements and circles for units of operation. As described, the flow chart should contain a stream split into two, with one part going to a mixing unit and the other part combined post-mixing. The mixed stream, consisting of DMEM, water, and bacteria, is fed into a filtration unit, after which it is mixed with FBS and PSG in a shaking unit. The final product is a growth medium.
02

Degree-of-feedom analysis

This step aims to determine the unknown variables for each piece of equipment. For each system, the degree of freedom (DOF) is calculated by the formula: DOF = n – e + 1, where n is the number of unknowns or variables and e is the number of independent equations. According to this, you'll have a specific DOF for the mixer, filter, shaker, splitter, the mixing point, and the overall system.
03

Calculating process variables

This step involves using mathematical techniques to solve for every unknown variable. Given the information about various inputs and outputs, together with known principles or equations (like mass balance), you should try to derive every unknown variable involved in the system.
04

Determining the mass ratio

This involves determining (i) the mass ratio of sterile growth medium product to feed water and (ii) the mass ratio of bacteria in the water to bacteria in the powder. Based on mass balance, the mass ratios can be calculated.
05

Reasons for bacteria removal

This is a reasoning step, and it should include two reasons for bacteria removal. An example of this could be to ensure the medium remains sterile and conducive to the growth of mammalian cells, and to prevent contamination that could alter the cell's function or damage the cells.

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Key Concepts

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

Mammalian Cell Culture
Mammalian cell culture involves the growth and maintenance of mammalian cells in a controlled environment. These cells are used for a variety of scientific and medical purposes, including vaccine production and research. To successfully grow mammalian cells, several essential conditions need to be met:

- A nurturing environment is essential, which mimics the natural conditions of the cells. - Nutrient-rich growth media is required, often supplemented with fetal bovine serum (FBS) which provides growth factors. - Sterility is crucial to prevent contamination that could damage the cells or alter their function.

Mammalian cell culture is a delicate process, requiring a balance of nutrient supply and contamination control to ensure that cells grow healthily and according to research or production requirements.
Degree-of-Freedom Analysis
Degree-of-freedom (DOF) analysis is a fundamental concept in chemical engineering, used to analyze systems of equations in regards to process variables. Typically expressed by the equation:\[ \text{DOF} = n - e + 1 \]where \( n \) is the number of unknown process variables and \( e \) is the number of independent equations available, this equation allows engineers to determine whether a system is solvable. If the DOF is zero, the process is deterministic and solvable. A positive DOF indicates a need for additional equations or data, while a negative DOF means the system is over-specified.

In the context of mammalian cell culture, DOF analysis helps identify which parts of the overall process—such as mixers, filters, or shakers—can be further explored to determine unknown process variables. This is important to ensure efficient design and operation of the chemical processes involved.
Sterile Growth Media
Sterile growth media is vital for supporting the healthy development of mammalian cells. This media provides essential nutrients and serves as a controlled environment free from unwanted microorganisms. The growth media consists of several key components:

- Water, which acts as a solvent and medium for reactions. - DMEM, a common powder containing sugars, amino acids, and other nutrients. - Fetal bovine serum (FBS) and antibiotic cocktails such as PSG to support growth and prevent contamination.

Maintaining sterility is paramount, as even slight bacterial, fungal, or yeast contamination can compromise cell growth. This is resolved through processes like filtration which remove unwanted microorganisms to ensure the medium remains conducive to cell culture.
Process Flowchart
A process flowchart is an essential tool in chemical process design. It visually represents the steps and flow of materials through a system. In the context of mammalian cell culture, a flowchart may include:

- Splitting of aqueous streams and their mixing with powdered substances in a mixer. - The movement of combined streams through a filtration unit to remove contaminants. - The final mixing with additional components like FBS and antibiotics to form a sterile culture medium.

The flowchart helps identify the sequence of processing units and materials involved, aiding in the understanding of how each part of the process contributes to the final product. It is crucial for engineers to draw precise, labeled flowcharts to efficiently communicate the setup and interactions within a chemical process.

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Most popular questions from this chapter

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.

A catalytic reactor is used to produce formaldehyde from methanol in the reaction $$\mathrm{CH}_{3} \mathrm{OH} \rightarrow \mathrm{HCHO}+\mathrm{H}_{2}$$ A single-pass conversion of \(60.0 \%\) is achieved in the reactor. The methanol in the reactor product is separated from the formaldehyde and hydrogen in a multiple-unit process. The production rate of formaldehyde is 900.0 kg/h. (a) Calculate the required feed rate of methanol to the process ( \(\mathrm{kmol} / \mathrm{h}\) ) if there is no recycle. (b) Suppose the unreacted methanol is recovered and recycled to the reactor and the single-pass conversion remains 60\%. Without doing any calculations, prove that you have enough information to determine the required fresh feed rate of methanol (kmol/h) and the rates (kmol/h) at which methanol enters and leaves the reactor. Then perform the calculations. (c) The single-pass conversion in the reactor, \(X_{\mathrm{sp}},\) affects the costs of the reactor \(\left(C_{\mathrm{r}}\right)\) and the separation process and recycle line \(\left(C_{\mathrm{s}}\right) .\) What effect would you expect an increased \(X_{\mathrm{sp}}\) would have on each of these costs for a fixed formaldehyde production rate? (Hint: To get a \(100 \%\) singlepass conversion you would need an infinitely large reactor, and lowering the single-pass conversion leads to a need to process greater amounts of fluid through both process units and the recycle line.) What would you expect a plot of \(\left(C_{\mathrm{r}}+C_{\mathrm{s}}\right)\) versus \(X_{\mathrm{sp}}\) to look like? What does the design specification \(X_{\mathrm{sp}}=60 \%\) probably represent?

A fuel oil is fed to a furnace and burned with \(25 \%\) excess air. The oil contains \(87.0 \mathrm{wt} \% \mathrm{C}, 10.0 \% \mathrm{H},\) and 3.0\% S. Analysis of the furnace exhaust gas shows only \(\mathrm{N}_{2}, \mathrm{O}_{2}, \mathrm{CO}_{2}, \mathrm{SO}_{2},\) and \(\mathrm{H}_{2} \mathrm{O}\). The sulfur dioxide emission rate is to be controlled by passing the exhaust gas through a scrubber, in which most of the \(\mathrm{SO}_{2}\) is absorbed in an alkaline solution. The gases leaving the scrubber (all of the \(\mathrm{N}_{2}, \mathrm{O}_{2},\) and \(\mathrm{CO}_{2}\), and some of the \(\mathrm{H}_{2} \mathrm{O}\) and \(\mathrm{SO}_{2}\) entering the unit) pass out to a stack. The scrubber has a limited capacity, however, so that a fraction of the furnace exhaust gas must be bypassed directly to the stack. At one point during the operation of the process, the scrubber removes \(90 \%\) of the \(\mathrm{SO}_{2}\) in the gas fed to it, and the combined stack gas contains 612.5 ppm (parts per million) \(\mathrm{SO}_{2}\) on a dry basis; that is, every million moles of dry stack gas contains 612.5 moles of \(\mathrm{SO}_{2}\). Calculate the fraction of the exhaust bypassing the scrubber at this moment.

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?

Ethylene oxide is produced by the catalytic oxidation of ethylene: $$ 2 \mathrm{C}_{2} \mathrm{H}_{4}+\mathrm{O}_{2} \longrightarrow 2 \mathrm{C}_{2} \mathrm{H}_{4} \mathrm{O} $$ An undesired competing reaction is the combustion of ethylene: $$ \mathrm{C}_{2} \mathrm{H}_{4}+3 \mathrm{O}_{2} \longrightarrow 2 \mathrm{CO}_{2}+2 \mathrm{H}_{2} \mathrm{O} $$ The feed to the reactor (not the fresh feed to the process) contains 3 moles of ethylene per mole of oxygen. The single-pass conversion of ethylene is \(20 \%,\) and for every 100 moles of ethylene consumed in the reactor, 90 moles of ethylene oxide emerge in the reactor products. A multiple-unit process is used to separate the products: ethylene and oxygen are recycled to the reactor, ethylene oxide is sold as a product, and carbon dioxide and water are discarded. (a) Assume a quantity of the reactor feed stream as a basis of calculation, draw and label the flowchart, perform a degree-of-freedom analysis, and write the equations you would use to calculate (i) the molar flow rates of ethylene and oxygen in the fresh feed, (ii) the production rate of ethylene oxide, and (iii) the overall conversion of ethylene. Do no calculations. (b) Calculate the quantities specified in Part (a), either manually or with an equation-solving program. (c) Calculate the molar flow rates of ethylene and oxygen in the fresh feed needed to produce 1 ton per hour of ethylene oxide.

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