/*! 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

In the production of a bean oil, beans containing 13.0 wt\% oil and \(87.0 \%\) solids are ground and fed to a stirred tank (the extractor) along with a recycled stream of liquid \(n\) -hexane. The feed ratio is \(3 \mathrm{kg}\) hexane/kg beans. The ground beans are suspended in the liquid, and essentially all of the oil in the beans is extracted into the hexane. The extractor effluent passes to a filter where the solids are collected and form a filter cake. The filter cake contains 75.0 wt\% bean solids and the balance bean oil and hexane, the latter two in the same ratio in which they emerge from the extractor. The filter cake is discarded and the liquid filtrate is fed to a heated evaporator in which the hexane is vaporized and the oil remains as a liquid. The oil is stored in drums and shipped. The hexane vapor is subsequently cooled and condensed, and the liquid hexane condensate is recycled to the extractor. (a) Draw and label a flowchart of the process, do the degree-of-freedom analysis, and write in an efficient order the equations you would solve to determine all unknown stream variables, circling the variables for which you would solve. (b) Calculate the yield of bean oil product (kg oil/kg beans fed), the required fresh hexane feed \(\left(\mathrm{kg} \mathrm{C}_{6} \mathrm{H}_{14} / \mathrm{kg} \text { beans fed }\right),\) and the recycle to fresh feed ratio (kg hexane recycled/kg fresh feed). (c) It has been suggested that a heat exchanger might be added to the process. This process unit would consist of a bundle of parallel metal tubes contained in an outer shell. The liquid filtrate would pass from the filter through the inside of the tubes and then go on to the evaporator. The hot hexane vapor on its way from the evaporator to the extractor would flow through the shell, passing over the outside of the tubes and heating the filtrate. How might the inclusion of this unit lead to a reduction in the operating cost of the process? (d) Suggest additional steps that might improve the process economics.

A mixture of propane and butane is burned with pure oxygen. The combustion products contain 47.4 mole \(\% \mathrm{H}_{2} \mathrm{O}\). After all the water is removed from the products, the residual gas contains 69.4 mole \(\% \mathrm{CO}_{2}\) and the balance \(\mathrm{O}_{2}\) (a) What is the mole percent of propane in the fuel? (b) It now turns out that the fuel mixture may contain not only propane and butane but also other hydrocarbons. All that is certain is that there is no oxygen in the fuel. Use atomic balances to calculate the elemental molar composition of the fuel from the given combustion product analysis (i.e., what mole percent is \(C\) and what percent is \(\mathrm{H}\) ). Prove that your solution is consistent with the result of Part (a).

Effluents from metal-finishing plants have the potential of discharging undesirable quantities of metals, such as cadmium, nickel, lead, manganese, and chromium, in forms that are detrimental to water and air quality. A local metal-finishing plant has identified a wastewater stream that contains 5.15 wt\% chromium (Cr) and devised the following approach to lowering risk and recovering the valuable metal. The wastewater stream is fed to a treatment unit that removes \(95 \%\) of the chromium in the feed and recycles it to the plant. The residual liquid stream leaving the treatment unit is sent to a waste lagoon. The treatment unit has a maximum capacity of 4500 kg wastewater/h. If wastewater leaves the finishing plant at a rate higher than the capacity of the treatment unit, the excess (anything above \(4500 \mathrm{kg} / \mathrm{h}\) ) bypasses the unit and combines with the residual liquid leaving the unit, and the combined stream goes to the waste lagoon. (a) Without assuming a basis of calculation, draw and label a flowchart of the process. (b) Wastewater leaves the finishing plant at a rate \(\dot{m}_{1}=6000 \mathrm{kg} / \mathrm{h}\). Calculate the flow rate of liquid to the waste lagoon, \(\dot{m}_{6}(\mathrm{kg} / \mathrm{h}),\) and the mass fraction of \(\mathrm{Cr}\) in this liquid, \(x_{6}(\mathrm{kg} \mathrm{Cr} / \mathrm{kg})\) (c) Calculate the flow rate of liquid to the waste lagoon and the mass fraction of Crin this liquid for \(\dot{m}_{1}\) varying from \(1000 \mathrm{kg} / \mathrm{h}\) to \(10,000 \mathrm{kg} / \mathrm{h}\) in \(1000 \mathrm{kg} / \mathrm{h}\) increments. Generate a plot of \(x_{6}\) versus \(\dot{m}_{1}\). (Suggestion: Use a spreadsheet for these calculations.) (d) The company has hired you as a consultant to help them determine whether or not to add capacity to the treatment unit to increase the recovery of chromium. What would you need to know to make this determination? (e) What concerns might need to be addressed regarding the waste lagoon?

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.

A mixture of 75 mole \(\%\) methane and 25 mole \(\%\) hydrogen is burned with \(25 \%\) excess air. Fractional conversions of \(90 \%\) of the methane and \(85 \%\) of the hydrogen are achieved; of the methane that reacts, \(95 \%\) reacts to form \(\mathrm{CO}_{2}\) and the balance reacts to form CO. The hot combustion product gas passes through a boiler in which heat transferred from the gas converts boiler feedwater into steam. (a) Calculate the concentration of \(\mathrm{CO}\) (ppm) in the stack gas. (b) The CO in the stack gas is a pollutant. Its concentration can be decreased by increasing the percent excess air fed to the furnace. Think of at least two costs of doing so. (Hint: The heat released by the combustion goes into heating the combustion products; the higher the combustion product temperature, the more steam is produced.)

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