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book Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler cover

Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler

Edition 2ISBN: 9780130819086
book Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler cover

Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler

Edition 2ISBN: 9780130819086
Exercise 10
Hybridoma cells immobilized on surfaces of Sephadex beads are used in a packed column for
production of monoclonoal antibodies (Mab). Hybridoma concentration is approximately
X = 5 g/l in the bed. The flow rate of the synthetic medium and glucose concentration are Hybridoma cells immobilized on surfaces of Sephadex beads are used in a packed column for production of monoclonoal antibodies (Mab). Hybridoma concentration is approximately X = 5 g/l in the bed. The flow rate of the synthetic medium and glucose concentration are   respectively. The rate constant for Mab formation is   Assume that there are no diffusion limitations and glucose is the rate limiting nutrient.  a. Determine the volume and the height of the packed bed for 95% glucose conversion. Bed diameter is    Neglect the growth of the hybridomas and assume first order ki- netics.  b. If    Mab/g glu, determine the effluent Mab concentration and the productivity of the system. respectively. The rate constant for Mab formation is Hybridoma cells immobilized on surfaces of Sephadex beads are used in a packed column for production of monoclonoal antibodies (Mab). Hybridoma concentration is approximately X = 5 g/l in the bed. The flow rate of the synthetic medium and glucose concentration are   respectively. The rate constant for Mab formation is   Assume that there are no diffusion limitations and glucose is the rate limiting nutrient.  a. Determine the volume and the height of the packed bed for 95% glucose conversion. Bed diameter is    Neglect the growth of the hybridomas and assume first order ki- netics.  b. If    Mab/g glu, determine the effluent Mab concentration and the productivity of the system. Assume that there are no diffusion limitations and glucose is the rate limiting nutrient.
a. Determine the volume and the height of the packed bed for 95% glucose conversion. Bed
diameter is
Hybridoma cells immobilized on surfaces of Sephadex beads are used in a packed column for production of monoclonoal antibodies (Mab). Hybridoma concentration is approximately X = 5 g/l in the bed. The flow rate of the synthetic medium and glucose concentration are   respectively. The rate constant for Mab formation is   Assume that there are no diffusion limitations and glucose is the rate limiting nutrient.  a. Determine the volume and the height of the packed bed for 95% glucose conversion. Bed diameter is    Neglect the growth of the hybridomas and assume first order ki- netics.  b. If    Mab/g glu, determine the effluent Mab concentration and the productivity of the system. Neglect the growth of the hybridomas and assume first order ki-
netics.
b. If
Hybridoma cells immobilized on surfaces of Sephadex beads are used in a packed column for production of monoclonoal antibodies (Mab). Hybridoma concentration is approximately X = 5 g/l in the bed. The flow rate of the synthetic medium and glucose concentration are   respectively. The rate constant for Mab formation is   Assume that there are no diffusion limitations and glucose is the rate limiting nutrient.  a. Determine the volume and the height of the packed bed for 95% glucose conversion. Bed diameter is    Neglect the growth of the hybridomas and assume first order ki- netics.  b. If    Mab/g glu, determine the effluent Mab concentration and the productivity of the system. Mab/g glu, determine the effluent Mab concentration and the productivity
of the system.
Explanation
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Cells of hybridoma are immobilized on su...

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Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler
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