Deck 13: Bioprocessconsiderations in Usingplant Cell Cultures

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The uptake of the auxin, indole acetic acid (or IAA), by suspension cultures of Parthenocis-
sus sp. is nearly zero order at 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water
is The uptake of the auxin, indole acetic acid (or IAA), by suspension cultures of Parthenocis- sus sp. is nearly zero order at 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is   Beads of calcium alginate are most conveniently made as spheres with a 4-mm diameter. Assume the beads are made 25% by volume of plant cells. Assume the plant cells are 90% water and that the diffusivity of IAA in the gel is the same as in water. If the ex- ternal concentration is maintained at 2 mmol, will IAA penetrate to the center of the bead?<div style=padding-top: 35px> Beads of calcium alginate are most conveniently made as spheres with a
4-mm diameter. Assume the beads are made 25% by volume of plant cells. Assume the plant
cells are 90% water and that the diffusivity of IAA in the gel is the same as in water. If the ex-
ternal concentration is maintained at 2 mmol, will IAA penetrate to the center of the bead?
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Question
Gel-immobilized cells of Papaver somniferum (opium poppy) can make codeine from
codeinone. The rate of codeinone uptake is first order, with a rate constant of Gel-immobilized cells of Papaver somniferum (opium poppy) can make codeine from codeinone. The rate of codeinone uptake is first order, with a rate constant of   cells dry weight-s. The diffusivity of codeinone in the gel is   For a gel particle of 4-mm diameter with a 25% volume loading of cells (95% water), what will be the effec- tiveness factor?<div style=padding-top: 35px> cells dry weight-s. The diffusivity of codeinone in the gel is Gel-immobilized cells of Papaver somniferum (opium poppy) can make codeine from codeinone. The rate of codeinone uptake is first order, with a rate constant of   cells dry weight-s. The diffusivity of codeinone in the gel is   For a gel particle of 4-mm diameter with a 25% volume loading of cells (95% water), what will be the effec- tiveness factor?<div style=padding-top: 35px> For a gel particle
of 4-mm diameter with a 25% volume loading of cells (95% water), what will be the effec-
tiveness factor?
Question
The The   of a small bubble column (2 l) has been measured as   at an airflow of 4 l/m in. If the rate of oxygen uptake by a culture of Catharanthus roseus is 0.2 mmol   dry weight-h and if the critical oxygen concentration must be above 10% of saturation (about 8 mg/l), what is the maximum concentration of cells that can be maintained in the reactor?<div style=padding-top: 35px> of a small bubble column (2 l) has been measured as The   of a small bubble column (2 l) has been measured as   at an airflow of 4 l/m in. If the rate of oxygen uptake by a culture of Catharanthus roseus is 0.2 mmol   dry weight-h and if the critical oxygen concentration must be above 10% of saturation (about 8 mg/l), what is the maximum concentration of cells that can be maintained in the reactor?<div style=padding-top: 35px> at an airflow of 4 l/m in.
If the rate of oxygen uptake by a culture of Catharanthus roseus is 0.2 mmol The   of a small bubble column (2 l) has been measured as   at an airflow of 4 l/m in. If the rate of oxygen uptake by a culture of Catharanthus roseus is 0.2 mmol   dry weight-h and if the critical oxygen concentration must be above 10% of saturation (about 8 mg/l), what is the maximum concentration of cells that can be maintained in the reactor?<div style=padding-top: 35px> dry
weight-h and if the critical oxygen concentration must be above 10% of saturation (about
8 mg/l), what is the maximum concentration of cells that can be maintained in the reactor?
Question
C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production
of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose
and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed:
Q = 1 l/h, Glucose in the feed: C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed: Q = 1 l/h, Glucose in the feed:   Plant Cell Concentration: X = 6 g/l reac. The rate constant for IA formation:   Column diameter:   Growth is negligible and Monod kinetics is valid. Determine the following: a. For 95% glucose conversion determine required hydraulic residence time, volume, and the height of the column b. If   glu, determine IA concentration in the effluent and the productivity.<div style=padding-top: 35px> Plant Cell Concentration: X = 6 g/l reac. The rate
constant for IA formation: C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed: Q = 1 l/h, Glucose in the feed:   Plant Cell Concentration: X = 6 g/l reac. The rate constant for IA formation:   Column diameter:   Growth is negligible and Monod kinetics is valid. Determine the following: a. For 95% glucose conversion determine required hydraulic residence time, volume, and the height of the column b. If   glu, determine IA concentration in the effluent and the productivity.<div style=padding-top: 35px> Column diameter: C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed: Q = 1 l/h, Glucose in the feed:   Plant Cell Concentration: X = 6 g/l reac. The rate constant for IA formation:   Column diameter:   Growth is negligible and Monod kinetics is valid. Determine the following: a. For 95% glucose conversion determine required hydraulic residence time, volume, and the height of the column b. If   glu, determine IA concentration in the effluent and the productivity.<div style=padding-top: 35px> Growth is negligible and Monod kinetics is valid. Determine the following:
a. For 95% glucose conversion determine required hydraulic residence time, volume, and
the height of the column
b. If
C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed: Q = 1 l/h, Glucose in the feed:   Plant Cell Concentration: X = 6 g/l reac. The rate constant for IA formation:   Column diameter:   Growth is negligible and Monod kinetics is valid. Determine the following: a. For 95% glucose conversion determine required hydraulic residence time, volume, and the height of the column b. If   glu, determine IA concentration in the effluent and the productivity.<div style=padding-top: 35px> glu, determine IA concentration in the effluent and the productivity.
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Deck 13: Bioprocessconsiderations in Usingplant Cell Cultures
1
The uptake of the auxin, indole acetic acid (or IAA), by suspension cultures of Parthenocis-
sus sp. is nearly zero order at 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water
is The uptake of the auxin, indole acetic acid (or IAA), by suspension cultures of Parthenocis- sus sp. is nearly zero order at 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is   Beads of calcium alginate are most conveniently made as spheres with a 4-mm diameter. Assume the beads are made 25% by volume of plant cells. Assume the plant cells are 90% water and that the diffusivity of IAA in the gel is the same as in water. If the ex- ternal concentration is maintained at 2 mmol, will IAA penetrate to the center of the bead? Beads of calcium alginate are most conveniently made as spheres with a
4-mm diameter. Assume the beads are made 25% by volume of plant cells. Assume the plant
cells are 90% water and that the diffusivity of IAA in the gel is the same as in water. If the ex-
ternal concentration is maintained at 2 mmol, will IAA penetrate to the center of the bead?
According to the given data:
The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min.
The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s.
Beads of calcium alginate make spheres with = 4-mm diameter.
Beads are made of = 25% by volume of plant cells.
The external concentration = 2 µmol.
Using equation 9.65 to see if According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. at According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. , Then the substrate concentration is calculated as below:
To calculate According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. for the bead:
Mass of cells/bead According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. = 0.88 mg dry wt/bead. According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead)
= 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/ According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. )
= 0.438×10 -3 µ mol/s-cm 3
From 9.65 According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. For, According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. 2 µ mol/cm 3 -0.584 µ mol/cm 3. According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. 1.4 µ mol/cm 3 at According to the given data: The uptake of auxin and indole acetic acid in the suspension culture of Parthenocisus sp. is zero order at = 1 nmol/mg dry cell weight-min. The diffusivity of IAA in water is = 5 x 10 -6 cm 2 /s. Beads of calcium alginate make spheres with = 4-mm diameter. Beads are made of = 25% by volume of plant cells. The external concentration = 2 µmol. Using equation 9.65 to see if   at   , Then the substrate concentration is calculated as below: To calculate   for the bead: Mass of cells/bead       = 0.88 mg dry wt/bead.   = (1 × 10 -³ µ mol/mg.min) (0.88 ng/ bead) = 0.88×10 -3 µ mol/min.bead (1 min/60 s)(1 bead/   ) = 0.438×10 -3 µ mol/s-cm 3 From 9.65   For,       2 µ mol/cm 3 -0.584 µ mol/cm 3.   1.4 µ mol/cm 3 at   Therefore, the answer is yes as it will penetrate into the center of the bead. Therefore, the answer is yes as it will penetrate into the center of the bead.
2
Gel-immobilized cells of Papaver somniferum (opium poppy) can make codeine from
codeinone. The rate of codeinone uptake is first order, with a rate constant of Gel-immobilized cells of Papaver somniferum (opium poppy) can make codeine from codeinone. The rate of codeinone uptake is first order, with a rate constant of   cells dry weight-s. The diffusivity of codeinone in the gel is   For a gel particle of 4-mm diameter with a 25% volume loading of cells (95% water), what will be the effec- tiveness factor? cells dry weight-s. The diffusivity of codeinone in the gel is Gel-immobilized cells of Papaver somniferum (opium poppy) can make codeine from codeinone. The rate of codeinone uptake is first order, with a rate constant of   cells dry weight-s. The diffusivity of codeinone in the gel is   For a gel particle of 4-mm diameter with a 25% volume loading of cells (95% water), what will be the effec- tiveness factor? For a gel particle
of 4-mm diameter with a 25% volume loading of cells (95% water), what will be the effec-
tiveness factor?
According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet.
Dry weight is = 5 %.
Mass of cells/bead = 0.44 mg/bead.
Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l
Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1
For, 0.4 cm diameter bead According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet. Dry weight is = 5 %. Mass of cells/bead = 0.44 mg/bead. Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1 For, 0.4 cm diameter bead   0.0335 cm 3 and   0.503 cm 2   First order so   Thus, for first order reaction       0.0306     Clearly, diffusional limitations is not important. 0.0335 cm 3 and According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet. Dry weight is = 5 %. Mass of cells/bead = 0.44 mg/bead. Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1 For, 0.4 cm diameter bead   0.0335 cm 3 and   0.503 cm 2   First order so   Thus, for first order reaction       0.0306     Clearly, diffusional limitations is not important. 0.503 cm 2 According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet. Dry weight is = 5 %. Mass of cells/bead = 0.44 mg/bead. Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1 For, 0.4 cm diameter bead   0.0335 cm 3 and   0.503 cm 2   First order so   Thus, for first order reaction       0.0306     Clearly, diffusional limitations is not important. First order so According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet. Dry weight is = 5 %. Mass of cells/bead = 0.44 mg/bead. Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1 For, 0.4 cm diameter bead   0.0335 cm 3 and   0.503 cm 2   First order so   Thus, for first order reaction       0.0306     Clearly, diffusional limitations is not important. Thus, for first order reaction According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet. Dry weight is = 5 %. Mass of cells/bead = 0.44 mg/bead. Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1 For, 0.4 cm diameter bead   0.0335 cm 3 and   0.503 cm 2   First order so   Thus, for first order reaction       0.0306     Clearly, diffusional limitations is not important. According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet. Dry weight is = 5 %. Mass of cells/bead = 0.44 mg/bead. Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1 For, 0.4 cm diameter bead   0.0335 cm 3 and   0.503 cm 2   First order so   Thus, for first order reaction       0.0306     Clearly, diffusional limitations is not important. According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet. Dry weight is = 5 %. Mass of cells/bead = 0.44 mg/bead. Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1 For, 0.4 cm diameter bead   0.0335 cm 3 and   0.503 cm 2   First order so   Thus, for first order reaction       0.0306     Clearly, diffusional limitations is not important. 0.0306 According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet. Dry weight is = 5 %. Mass of cells/bead = 0.44 mg/bead. Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1 For, 0.4 cm diameter bead   0.0335 cm 3 and   0.503 cm 2   First order so   Thus, for first order reaction       0.0306     Clearly, diffusional limitations is not important. According to the equation 9.63. The first order reaction constant needs to be based on the whole pellet. Dry weight is = 5 %. Mass of cells/bead = 0.44 mg/bead. Cell concentration = 0.44 mg/0.0335 cm 3 = 13.1 g/l Thus the rate constant is k = 3.3 × 10 -8 (13.1) = 4.3 × 10 -7 s -1 For, 0.4 cm diameter bead   0.0335 cm 3 and   0.503 cm 2   First order so   Thus, for first order reaction       0.0306     Clearly, diffusional limitations is not important. Clearly, diffusional limitations is not important.
3
The The   of a small bubble column (2 l) has been measured as   at an airflow of 4 l/m in. If the rate of oxygen uptake by a culture of Catharanthus roseus is 0.2 mmol   dry weight-h and if the critical oxygen concentration must be above 10% of saturation (about 8 mg/l), what is the maximum concentration of cells that can be maintained in the reactor? of a small bubble column (2 l) has been measured as The   of a small bubble column (2 l) has been measured as   at an airflow of 4 l/m in. If the rate of oxygen uptake by a culture of Catharanthus roseus is 0.2 mmol   dry weight-h and if the critical oxygen concentration must be above 10% of saturation (about 8 mg/l), what is the maximum concentration of cells that can be maintained in the reactor? at an airflow of 4 l/m in.
If the rate of oxygen uptake by a culture of Catharanthus roseus is 0.2 mmol The   of a small bubble column (2 l) has been measured as   at an airflow of 4 l/m in. If the rate of oxygen uptake by a culture of Catharanthus roseus is 0.2 mmol   dry weight-h and if the critical oxygen concentration must be above 10% of saturation (about 8 mg/l), what is the maximum concentration of cells that can be maintained in the reactor? dry
weight-h and if the critical oxygen concentration must be above 10% of saturation (about
8 mg/l), what is the maximum concentration of cells that can be maintained in the reactor?
Fom the equation 10.1: The maximum concentration of cells is: Fom the equation 10.1: The maximum concentration of cells is:   According to the given data:   8 mg/l.   0.10       0.2 m mol O 2 / g dry wt-h    According to the given data: Fom the equation 10.1: The maximum concentration of cells is:   According to the given data:   8 mg/l.   0.10       0.2 m mol O 2 / g dry wt-h    8 mg/l. Fom the equation 10.1: The maximum concentration of cells is:   According to the given data:   8 mg/l.   0.10       0.2 m mol O 2 / g dry wt-h    0.10 Fom the equation 10.1: The maximum concentration of cells is:   According to the given data:   8 mg/l.   0.10       0.2 m mol O 2 / g dry wt-h    Fom the equation 10.1: The maximum concentration of cells is:   According to the given data:   8 mg/l.   0.10       0.2 m mol O 2 / g dry wt-h    Fom the equation 10.1: The maximum concentration of cells is:   According to the given data:   8 mg/l.   0.10       0.2 m mol O 2 / g dry wt-h    0.2 m mol O 2 / g dry wt-h Fom the equation 10.1: The maximum concentration of cells is:   According to the given data:   8 mg/l.   0.10       0.2 m mol O 2 / g dry wt-h    Fom the equation 10.1: The maximum concentration of cells is:   According to the given data:   8 mg/l.   0.10       0.2 m mol O 2 / g dry wt-h
4
C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production
of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose
and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed:
Q = 1 l/h, Glucose in the feed: C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed: Q = 1 l/h, Glucose in the feed:   Plant Cell Concentration: X = 6 g/l reac. The rate constant for IA formation:   Column diameter:   Growth is negligible and Monod kinetics is valid. Determine the following: a. For 95% glucose conversion determine required hydraulic residence time, volume, and the height of the column b. If   glu, determine IA concentration in the effluent and the productivity. Plant Cell Concentration: X = 6 g/l reac. The rate
constant for IA formation: C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed: Q = 1 l/h, Glucose in the feed:   Plant Cell Concentration: X = 6 g/l reac. The rate constant for IA formation:   Column diameter:   Growth is negligible and Monod kinetics is valid. Determine the following: a. For 95% glucose conversion determine required hydraulic residence time, volume, and the height of the column b. If   glu, determine IA concentration in the effluent and the productivity. Column diameter: C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed: Q = 1 l/h, Glucose in the feed:   Plant Cell Concentration: X = 6 g/l reac. The rate constant for IA formation:   Column diameter:   Growth is negligible and Monod kinetics is valid. Determine the following: a. For 95% glucose conversion determine required hydraulic residence time, volume, and the height of the column b. If   glu, determine IA concentration in the effluent and the productivity. Growth is negligible and Monod kinetics is valid. Determine the following:
a. For 95% glucose conversion determine required hydraulic residence time, volume, and
the height of the column
b. If
C. roseus cells immobilized in Ca-alginate beads of diameter 0.5 mm are used for production of indole alkaloids (IA) in a fluidized-bed bioreactor. The rate limiting nutrient is glucose and no intraparticle diffusion limitations exist. Use the following data: Flow rate of the feed: Q = 1 l/h, Glucose in the feed:   Plant Cell Concentration: X = 6 g/l reac. The rate constant for IA formation:   Column diameter:   Growth is negligible and Monod kinetics is valid. Determine the following: a. For 95% glucose conversion determine required hydraulic residence time, volume, and the height of the column b. If   glu, determine IA concentration in the effluent and the productivity. glu, determine IA concentration in the effluent and the productivity.
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