Deck 14: Utilizing Geneticallyengineered Organisms

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Question
Assume that all plasmid-containing cells have eight plasmids; that an antibiotic is present in
the medium, and the plasmid-containing cells are totally resistant; and that a newly born,
plasmid-free cell has sufficient enzyme to protect a cell and its progeny for three generations.
Estimate the fraction of plasmid-containing cells in the population in a batch reactor starting
with only plasmid-containing cells after five generations.
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Question
Consider an industrial-scale batch fermentation. A 10,000 l fermenter with Consider an industrial-scale batch fermentation. A 10,000 l fermenter with   cells/ml is the desired scale-up operation. Inoculum for the large tank is brought through a series of seed tanks and flasks, beginning with a single pure colony growing on an agar slant. Assume that a colony   plasmid-containing cells) is picked and placed in a test tube with 1 ml of medium. Calculate how many generations will be required to achieve the required cell den- sity in the 10,000 l fermenter. What fraction of the total population will be plasmid-free cells  <div style=padding-top: 35px> cells/ml
is the desired scale-up operation. Inoculum for the large tank is brought through a series of
seed tanks and flasks, beginning with a single pure colony growing on an agar slant. Assume
that a colony Consider an industrial-scale batch fermentation. A 10,000 l fermenter with   cells/ml is the desired scale-up operation. Inoculum for the large tank is brought through a series of seed tanks and flasks, beginning with a single pure colony growing on an agar slant. Assume that a colony   plasmid-containing cells) is picked and placed in a test tube with 1 ml of medium. Calculate how many generations will be required to achieve the required cell den- sity in the 10,000 l fermenter. What fraction of the total population will be plasmid-free cells  <div style=padding-top: 35px> plasmid-containing cells) is picked and placed in a test tube with 1 ml of
medium. Calculate how many generations will be required to achieve the required cell den-
sity in the 10,000 l fermenter. What fraction of the total population will be plasmid-free cells Consider an industrial-scale batch fermentation. A 10,000 l fermenter with   cells/ml is the desired scale-up operation. Inoculum for the large tank is brought through a series of seed tanks and flasks, beginning with a single pure colony growing on an agar slant. Assume that a colony   plasmid-containing cells) is picked and placed in a test tube with 1 ml of medium. Calculate how many generations will be required to achieve the required cell den- sity in the 10,000 l fermenter. What fraction of the total population will be plasmid-free cells  <div style=padding-top: 35px>
Question
Assume that you have been assigned to a team to produce human epidermal growth factor
(hEGF). A small peptide, hEGF speeds wound healing and may be useful in treating ulcers. A
market size of 50 to 500 kg/yr has been estimated. Posttranslational processing is not essen-
tial to the value of the product. It is a secreted product in the natural host cell. Discuss what
recommendations you would make to the molecular-biology team leader for the choice of
host cell and the design of a reactor. Make your recommendations from the perspective of
what is desirable to make an effective process. You should point out any potential prob-
lems with the solution you have proposed, as well as defend why your approach should be
advantageous.
Question
Develop a model to describe the stability of a chemostat culture for a plasmid-containing cul-
ture. For some cultures, plasmids make a protein product (e.g., colicin in E. coli) that kills
plasmid-free cells but does not act on plasmid-containing cells. Assume that the rate of
killing by colicin is Develop a model to describe the stability of a chemostat culture for a plasmid-containing cul- ture. For some cultures, plasmids make a protein product (e.g., colicin in E. coli) that kills plasmid-free cells but does not act on plasmid-containing cells. Assume that the rate of killing by colicin is   where   is the rate constant for the killing and C is the colicin concentration. Assume that the colicin production is first order with respect to  <div style=padding-top: 35px> where Develop a model to describe the stability of a chemostat culture for a plasmid-containing cul- ture. For some cultures, plasmids make a protein product (e.g., colicin in E. coli) that kills plasmid-free cells but does not act on plasmid-containing cells. Assume that the rate of killing by colicin is   where   is the rate constant for the killing and C is the colicin concentration. Assume that the colicin production is first order with respect to  <div style=padding-top: 35px> is the rate constant for the killing and C is the colicin
concentration. Assume that the colicin production is first order with respect to Develop a model to describe the stability of a chemostat culture for a plasmid-containing cul- ture. For some cultures, plasmids make a protein product (e.g., colicin in E. coli) that kills plasmid-free cells but does not act on plasmid-containing cells. Assume that the rate of killing by colicin is   where   is the rate constant for the killing and C is the colicin concentration. Assume that the colicin production is first order with respect to  <div style=padding-top: 35px>
Question
Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple-
mented with amino acids. Estimate Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple- mented with amino acids. Estimate   and R. Compare the stability of this system to one with a glucose-minimal medium (Example 14.2). Example 14.2. The data in Table 14.4   were obtained for E. coli B/r-pDW17 at two different dilution rates in glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50 copies per cell. About 12<font face=symbol></font>of the total protein synthesized is due to the plasmid. The proteins are retained intracellularly in soluble form. Use these data to estimate    <div style=padding-top: 35px> and R. Compare the stability of this system to one
with a glucose-minimal medium (Example 14.2).
Example 14.2.
The data in Table 14.4 Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple- mented with amino acids. Estimate   and R. Compare the stability of this system to one with a glucose-minimal medium (Example 14.2). Example 14.2. The data in Table 14.4   were obtained for E. coli B/r-pDW17 at two different dilution rates in glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50 copies per cell. About 12<font face=symbol></font>of the total protein synthesized is due to the plasmid. The proteins are retained intracellularly in soluble form. Use these data to estimate    <div style=padding-top: 35px> were obtained for E. coli B/r-pDW17 at two different dilution rates in
glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50
copies per cell. About 12of the total protein synthesized is due to the plasmid. The proteins
are retained intracellularly in soluble form. Use these data to estimate Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple- mented with amino acids. Estimate   and R. Compare the stability of this system to one with a glucose-minimal medium (Example 14.2). Example 14.2. The data in Table 14.4   were obtained for E. coli B/r-pDW17 at two different dilution rates in glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50 copies per cell. About 12<font face=symbol></font>of the total protein synthesized is due to the plasmid. The proteins are retained intracellularly in soluble form. Use these data to estimate    <div style=padding-top: 35px> Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple- mented with amino acids. Estimate   and R. Compare the stability of this system to one with a glucose-minimal medium (Example 14.2). Example 14.2. The data in Table 14.4   were obtained for E. coli B/r-pDW17 at two different dilution rates in glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50 copies per cell. About 12<font face=symbol></font>of the total protein synthesized is due to the plasmid. The proteins are retained intracellularly in soluble form. Use these data to estimate    <div style=padding-top: 35px>
Question
It has been claimed that gel immobilization stabilizes a plasmid-containing population. A fac-
tor suggested to be responsible for the stabilization is compartmentalization of the population
into very small pockets. For example, the pocket may start with an individual cell and grow
to a level of 200 cells per cavity. Develop a mathematical formula to compare the number of
plasmid-free cells in a gel to that in a large, well-mixed tank.
Question
You must design an operating strategy to allow an E. coli fermentation to achieve a high cell
density You must design an operating strategy to allow an E. coli fermentation to achieve a high cell density   in a fed-batch system. You have access to an off-gas analyzer that will mea- sure the pCO₂ in the exit gas. The glucose concentration must be less than 100 mg/l to avoid the formation of acetate and other inhibitory products. Develop an approach to control the glucose feed rate so as to maintain the glucose level at   what equations would you use and what assumptions would you make?<div style=padding-top: 35px> in a fed-batch system. You have access to an off-gas analyzer that will mea-
sure the pCO₂ in the exit gas. The glucose concentration must be less than 100 mg/l to avoid
the formation of acetate and other inhibitory products. Develop an approach to control the
glucose feed rate so as to maintain the glucose level at You must design an operating strategy to allow an E. coli fermentation to achieve a high cell density   in a fed-batch system. You have access to an off-gas analyzer that will mea- sure the pCO₂ in the exit gas. The glucose concentration must be less than 100 mg/l to avoid the formation of acetate and other inhibitory products. Develop an approach to control the glucose feed rate so as to maintain the glucose level at   what equations would you use and what assumptions would you make?<div style=padding-top: 35px> what equations would
you use and what assumptions would you make?
Question
Develop a simple model for a population in which plasmids are present at division with copy
numbers 2, 4, 6, 8, or 10. The model should be developed in analogy to eqs. 14.7 through 14.9. You can assume that dividing cells either segregate plasmids perfectly or generate a
plasmid-free cell.
Question
Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells
in a 2 l reactor with a total cell population of Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells in a 2 l reactor with a total cell population of   cells/ml. You use this inoculum for a 1000 l reactor and achieve a final population of   cells/ml. Assuming     and P = 0.0002, predict the fraction of plasmid-containing cells.<div style=padding-top: 35px> cells/ml. You use this inoculum for a
1000 l reactor and achieve a final population of Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells in a 2 l reactor with a total cell population of   cells/ml. You use this inoculum for a 1000 l reactor and achieve a final population of   cells/ml. Assuming     and P = 0.0002, predict the fraction of plasmid-containing cells.<div style=padding-top: 35px> cells/ml. Assuming Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells in a 2 l reactor with a total cell population of   cells/ml. You use this inoculum for a 1000 l reactor and achieve a final population of   cells/ml. Assuming     and P = 0.0002, predict the fraction of plasmid-containing cells.<div style=padding-top: 35px> Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells in a 2 l reactor with a total cell population of   cells/ml. You use this inoculum for a 1000 l reactor and achieve a final population of   cells/ml. Assuming     and P = 0.0002, predict the fraction of plasmid-containing cells.<div style=padding-top: 35px> and P = 0.0002, predict the fraction of plasmid-containing cells.
Question
Assume you scale up from Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest?<div style=padding-top: 35px> cells/ml of 100% plasmid-containing cells to Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest?<div style=padding-top: 35px> cells/ml, at which point overproduction of the target protein is induced. Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest?<div style=padding-top: 35px> You harvest six hours after induction. The value of P is 0.0005. Before induction Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest?<div style=padding-top: 35px> Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest?<div style=padding-top: 35px> After induction Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest?<div style=padding-top: 35px> What is the fraction of plasmid-
containing cells at induction? What is the fraction of plasmid-containing cells at harvest?
Question
Given the following information, calculate the probability of forming a plasmid-free cell due
to random segregation for a cell with 50 plasmid monomer equivalents:
a. 40% of the total plasmid DNA is in dimers and 16% in tetramers.
b. The distribution of copy numbers per cell is as follows, assuming monomers only:
Given the following information, calculate the probability of forming a plasmid-free cell due to random segregation for a cell with 50 plasmid monomer equivalents: a. 40% of the total plasmid DNA is in dimers and 16% in tetramers. b. The distribution of copy numbers per cell is as follows, assuming monomers only:  <div style=padding-top: 35px>
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Deck 14: Utilizing Geneticallyengineered Organisms
1
Assume that all plasmid-containing cells have eight plasmids; that an antibiotic is present in
the medium, and the plasmid-containing cells are totally resistant; and that a newly born,
plasmid-free cell has sufficient enzyme to protect a cell and its progeny for three generations.
Estimate the fraction of plasmid-containing cells in the population in a batch reactor starting
with only plasmid-containing cells after five generations.
According to the given data:
As a basis, for the calculation assuming According to the given data: As a basis, for the calculation assuming   that   and   Further   for   where i = 1, 2, or 3;   = dead cell   0.00781 plasmid-free cells / division   0.008   Total plasmid-free cells = 563 or 1.76% Total Viable plasmid-free cells = 371 or 1.16% Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16% that According to the given data: As a basis, for the calculation assuming   that   and   Further   for   where i = 1, 2, or 3;   = dead cell   0.00781 plasmid-free cells / division   0.008   Total plasmid-free cells = 563 or 1.76% Total Viable plasmid-free cells = 371 or 1.16% Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16% and According to the given data: As a basis, for the calculation assuming   that   and   Further   for   where i = 1, 2, or 3;   = dead cell   0.00781 plasmid-free cells / division   0.008   Total plasmid-free cells = 563 or 1.76% Total Viable plasmid-free cells = 371 or 1.16% Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16%
Further According to the given data: As a basis, for the calculation assuming   that   and   Further   for   where i = 1, 2, or 3;   = dead cell   0.00781 plasmid-free cells / division   0.008   Total plasmid-free cells = 563 or 1.76% Total Viable plasmid-free cells = 371 or 1.16% Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16% for According to the given data: As a basis, for the calculation assuming   that   and   Further   for   where i = 1, 2, or 3;   = dead cell   0.00781 plasmid-free cells / division   0.008   Total plasmid-free cells = 563 or 1.76% Total Viable plasmid-free cells = 371 or 1.16% Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16% where i = 1, 2, or 3; According to the given data: As a basis, for the calculation assuming   that   and   Further   for   where i = 1, 2, or 3;   = dead cell   0.00781 plasmid-free cells / division   0.008   Total plasmid-free cells = 563 or 1.76% Total Viable plasmid-free cells = 371 or 1.16% Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16% = dead cell According to the given data: As a basis, for the calculation assuming   that   and   Further   for   where i = 1, 2, or 3;   = dead cell   0.00781 plasmid-free cells / division   0.008   Total plasmid-free cells = 563 or 1.76% Total Viable plasmid-free cells = 371 or 1.16% Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16% 0.00781 plasmid-free cells / division According to the given data: As a basis, for the calculation assuming   that   and   Further   for   where i = 1, 2, or 3;   = dead cell   0.00781 plasmid-free cells / division   0.008   Total plasmid-free cells = 563 or 1.76% Total Viable plasmid-free cells = 371 or 1.16% Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16% 0.008 According to the given data: As a basis, for the calculation assuming   that   and   Further   for   where i = 1, 2, or 3;   = dead cell   0.00781 plasmid-free cells / division   0.008   Total plasmid-free cells = 563 or 1.76% Total Viable plasmid-free cells = 371 or 1.16% Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16% Total plasmid-free cells = 563 or 1.76%
Total Viable plasmid-free cells = 371 or 1.16%
Thus, the total plasmid-free cells are found to be 1.70% and viable plasmid-free cell is found to be 1.16%
2
Consider an industrial-scale batch fermentation. A 10,000 l fermenter with Consider an industrial-scale batch fermentation. A 10,000 l fermenter with   cells/ml is the desired scale-up operation. Inoculum for the large tank is brought through a series of seed tanks and flasks, beginning with a single pure colony growing on an agar slant. Assume that a colony   plasmid-containing cells) is picked and placed in a test tube with 1 ml of medium. Calculate how many generations will be required to achieve the required cell den- sity in the 10,000 l fermenter. What fraction of the total population will be plasmid-free cells  cells/ml
is the desired scale-up operation. Inoculum for the large tank is brought through a series of
seed tanks and flasks, beginning with a single pure colony growing on an agar slant. Assume
that a colony Consider an industrial-scale batch fermentation. A 10,000 l fermenter with   cells/ml is the desired scale-up operation. Inoculum for the large tank is brought through a series of seed tanks and flasks, beginning with a single pure colony growing on an agar slant. Assume that a colony   plasmid-containing cells) is picked and placed in a test tube with 1 ml of medium. Calculate how many generations will be required to achieve the required cell den- sity in the 10,000 l fermenter. What fraction of the total population will be plasmid-free cells  plasmid-containing cells) is picked and placed in a test tube with 1 ml of
medium. Calculate how many generations will be required to achieve the required cell den-
sity in the 10,000 l fermenter. What fraction of the total population will be plasmid-free cells Consider an industrial-scale batch fermentation. A 10,000 l fermenter with   cells/ml is the desired scale-up operation. Inoculum for the large tank is brought through a series of seed tanks and flasks, beginning with a single pure colony growing on an agar slant. Assume that a colony   plasmid-containing cells) is picked and placed in a test tube with 1 ml of medium. Calculate how many generations will be required to achieve the required cell den- sity in the 10,000 l fermenter. What fraction of the total population will be plasmid-free cells
According to the given data:
In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml.
A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells.
The number of generations required for a cell density = 10,000 l.
To calculate the total number of cells: According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. Final cell = According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. Therefore, generations According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. = 39
According to the given data, using equation 14.51 to calculate According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. the following calculation is evolved: According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. µ + = 1.0 h -1
µ - = 1.2 h -1 According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. According to the given data: In industrial-scale batch fementtion 10,000 l fermenter has = 5 × 10 10 cells/ml. A colony is picked and placed in test tube of 1 ml = 10 6 plasmid-containing cells. The number of generations required for a cell density = 10,000 l. To calculate the total number of cells:   Final cell =     Therefore, generations   = 39 According to the given data, using equation 14.51 to calculate   the following calculation is evolved:   µ + = 1.0 h -1 µ - = 1.2 h -1             = 0.36. Thus, the fraction of total population in plasmid-free cells is 0.36. = 0.36.
Thus, the fraction of total population in plasmid-free cells is 0.36.
3
Assume that you have been assigned to a team to produce human epidermal growth factor
(hEGF). A small peptide, hEGF speeds wound healing and may be useful in treating ulcers. A
market size of 50 to 500 kg/yr has been estimated. Posttranslational processing is not essen-
tial to the value of the product. It is a secreted product in the natural host cell. Discuss what
recommendations you would make to the molecular-biology team leader for the choice of
host cell and the design of a reactor. Make your recommendations from the perspective of
what is desirable to make an effective process. You should point out any potential prob-
lems with the solution you have proposed, as well as defend why your approach should be
advantageous.
Human epidermal growth factor (hEGF) is assigned to a tem. The growth factor increase the healing and are useful in treating ulcers.
Several choices could be well defined. Since, post-translational processing is not required, efficiency and productivity has become critical. If the protein can be resolublized from inclusion bodies, then E.coli will likely be the best choice, if intracellular degradation is not a problem.
An E.coli system modified, for excretion would be advantageous. Yeast or fungal systems would also be possible alternatives particularly, for internal medical use.
4
Develop a model to describe the stability of a chemostat culture for a plasmid-containing cul-
ture. For some cultures, plasmids make a protein product (e.g., colicin in E. coli) that kills
plasmid-free cells but does not act on plasmid-containing cells. Assume that the rate of
killing by colicin is Develop a model to describe the stability of a chemostat culture for a plasmid-containing cul- ture. For some cultures, plasmids make a protein product (e.g., colicin in E. coli) that kills plasmid-free cells but does not act on plasmid-containing cells. Assume that the rate of killing by colicin is   where   is the rate constant for the killing and C is the colicin concentration. Assume that the colicin production is first order with respect to  where Develop a model to describe the stability of a chemostat culture for a plasmid-containing cul- ture. For some cultures, plasmids make a protein product (e.g., colicin in E. coli) that kills plasmid-free cells but does not act on plasmid-containing cells. Assume that the rate of killing by colicin is   where   is the rate constant for the killing and C is the colicin concentration. Assume that the colicin production is first order with respect to  is the rate constant for the killing and C is the colicin
concentration. Assume that the colicin production is first order with respect to Develop a model to describe the stability of a chemostat culture for a plasmid-containing cul- ture. For some cultures, plasmids make a protein product (e.g., colicin in E. coli) that kills plasmid-free cells but does not act on plasmid-containing cells. Assume that the rate of killing by colicin is   where   is the rate constant for the killing and C is the colicin concentration. Assume that the colicin production is first order with respect to
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5
Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple-
mented with amino acids. Estimate Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple- mented with amino acids. Estimate   and R. Compare the stability of this system to one with a glucose-minimal medium (Example 14.2). Example 14.2. The data in Table 14.4   were obtained for E. coli B/r-pDW17 at two different dilution rates in glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50 copies per cell. About 12<font face=symbol></font>of the total protein synthesized is due to the plasmid. The proteins are retained intracellularly in soluble form. Use these data to estimate    and R. Compare the stability of this system to one
with a glucose-minimal medium (Example 14.2).
Example 14.2.
The data in Table 14.4 Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple- mented with amino acids. Estimate   and R. Compare the stability of this system to one with a glucose-minimal medium (Example 14.2). Example 14.2. The data in Table 14.4   were obtained for E. coli B/r-pDW17 at two different dilution rates in glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50 copies per cell. About 12<font face=symbol></font>of the total protein synthesized is due to the plasmid. The proteins are retained intracellularly in soluble form. Use these data to estimate    were obtained for E. coli B/r-pDW17 at two different dilution rates in
glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50
copies per cell. About 12of the total protein synthesized is due to the plasmid. The proteins
are retained intracellularly in soluble form. Use these data to estimate Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple- mented with amino acids. Estimate   and R. Compare the stability of this system to one with a glucose-minimal medium (Example 14.2). Example 14.2. The data in Table 14.4   were obtained for E. coli B/r-pDW17 at two different dilution rates in glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50 copies per cell. About 12<font face=symbol></font>of the total protein synthesized is due to the plasmid. The proteins are retained intracellularly in soluble form. Use these data to estimate    Consider the following data for E. coli B/r-pDW17 grown in a minimal medium supple- mented with amino acids. Estimate   and R. Compare the stability of this system to one with a glucose-minimal medium (Example 14.2). Example 14.2. The data in Table 14.4   were obtained for E. coli B/r-pDW17 at two different dilution rates in glucose-limited chemostats. The average plasmid copy number for pDW17 is about 40 to 50 copies per cell. About 12<font face=symbol></font>of the total protein synthesized is due to the plasmid. The proteins are retained intracellularly in soluble form. Use these data to estimate
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6
It has been claimed that gel immobilization stabilizes a plasmid-containing population. A fac-
tor suggested to be responsible for the stabilization is compartmentalization of the population
into very small pockets. For example, the pocket may start with an individual cell and grow
to a level of 200 cells per cavity. Develop a mathematical formula to compare the number of
plasmid-free cells in a gel to that in a large, well-mixed tank.
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7
You must design an operating strategy to allow an E. coli fermentation to achieve a high cell
density You must design an operating strategy to allow an E. coli fermentation to achieve a high cell density   in a fed-batch system. You have access to an off-gas analyzer that will mea- sure the pCO₂ in the exit gas. The glucose concentration must be less than 100 mg/l to avoid the formation of acetate and other inhibitory products. Develop an approach to control the glucose feed rate so as to maintain the glucose level at   what equations would you use and what assumptions would you make? in a fed-batch system. You have access to an off-gas analyzer that will mea-
sure the pCO₂ in the exit gas. The glucose concentration must be less than 100 mg/l to avoid
the formation of acetate and other inhibitory products. Develop an approach to control the
glucose feed rate so as to maintain the glucose level at You must design an operating strategy to allow an E. coli fermentation to achieve a high cell density   in a fed-batch system. You have access to an off-gas analyzer that will mea- sure the pCO₂ in the exit gas. The glucose concentration must be less than 100 mg/l to avoid the formation of acetate and other inhibitory products. Develop an approach to control the glucose feed rate so as to maintain the glucose level at   what equations would you use and what assumptions would you make? what equations would
you use and what assumptions would you make?
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8
Develop a simple model for a population in which plasmids are present at division with copy
numbers 2, 4, 6, 8, or 10. The model should be developed in analogy to eqs. 14.7 through 14.9. You can assume that dividing cells either segregate plasmids perfectly or generate a
plasmid-free cell.
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9
Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells
in a 2 l reactor with a total cell population of Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells in a 2 l reactor with a total cell population of   cells/ml. You use this inoculum for a 1000 l reactor and achieve a final population of   cells/ml. Assuming     and P = 0.0002, predict the fraction of plasmid-containing cells. cells/ml. You use this inoculum for a
1000 l reactor and achieve a final population of Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells in a 2 l reactor with a total cell population of   cells/ml. You use this inoculum for a 1000 l reactor and achieve a final population of   cells/ml. Assuming     and P = 0.0002, predict the fraction of plasmid-containing cells. cells/ml. Assuming Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells in a 2 l reactor with a total cell population of   cells/ml. You use this inoculum for a 1000 l reactor and achieve a final population of   cells/ml. Assuming     and P = 0.0002, predict the fraction of plasmid-containing cells. Assume you have an inoculum with 95% plasmid-containing cells and 5% plasmid-free cells in a 2 l reactor with a total cell population of   cells/ml. You use this inoculum for a 1000 l reactor and achieve a final population of   cells/ml. Assuming     and P = 0.0002, predict the fraction of plasmid-containing cells. and P = 0.0002, predict the fraction of plasmid-containing cells.
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10
Assume you scale up from Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest? cells/ml of 100% plasmid-containing cells to Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest? cells/ml, at which point overproduction of the target protein is induced. Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest? You harvest six hours after induction. The value of P is 0.0005. Before induction Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest? Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest? After induction Assume you scale up from   cells/ml of 100% plasmid-containing cells to   cells/ml, at which point overproduction of the target protein is induced.   You harvest six hours after induction. The value of P is 0.0005. Before induction     After induction   What is the fraction of plasmid- containing cells at induction? What is the fraction of plasmid-containing cells at harvest? What is the fraction of plasmid-
containing cells at induction? What is the fraction of plasmid-containing cells at harvest?
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11
Given the following information, calculate the probability of forming a plasmid-free cell due
to random segregation for a cell with 50 plasmid monomer equivalents:
a. 40% of the total plasmid DNA is in dimers and 16% in tetramers.
b. The distribution of copy numbers per cell is as follows, assuming monomers only:
Given the following information, calculate the probability of forming a plasmid-free cell due to random segregation for a cell with 50 plasmid monomer equivalents: a. 40% of the total plasmid DNA is in dimers and 16% in tetramers. b. The distribution of copy numbers per cell is as follows, assuming monomers only:
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