recategorized by
0 0 votes

In a fed-batch culture, $200 \text{ g . L}^{-1}$ glucose solution is added at a flow rate of $50 \text{ L . h}^{-1}$ . The initial culture volume (at quasi steady state) and the initial cell concentration are $600 \: L$ and $20 \text{g . L}^{-1}$ , respectively. The yield coefficient $(Y_{x/s})$ is $0.5\: g $ cell mass.g substrate$^{-1}$. The cell concentration $g . L^{-1})$ at quasi steady state at $t=8 \:h$ is

  1. $40$
  2. $52$
  3. $60$
  4. $68$

Please log in or register to answer this question.

Answer:

Related questions

0 0 votes
0 0 answers
Milicevic3306 asked Mar 26, 2018
Oxygen transfer was measured in a stirred tank bioreactor using dynamic method. The dissolved oxygen tension was found to be $80 \%$ air saturation under steady state con...
0 0 votes
0 0 answers
Milicevic3306 asked Mar 26, 2018
Biomass is being produced in a continuous stirred tank bioreactor of $750$ L capacity. The sterile feed containing $8 \: g \cdot L^{-1}$ glucose as substrate was fed at a...
0 0 votes
0 0 answers
Milicevic3306 asked Mar 26, 2018
The diameters of a large and a small vessel are $1.62$ m and $16.2$ cm. ,respectively. The vessels are geometrically similar and operated under similar volumetric agitate...
0 0 votes
0 0 answers
Milicevic3306 asked Mar 26, 2018
$\textit{Saccharomyces cerevisiae}$ produces ethanol by fermentation. The theoretical yield of ethanol from $2.5$ g of glucose is _________ g.
0 0 votes
0 0 answers
gatecse asked Feb 23
A $\text{CSTR}$ with a volume of $100 \mathrm{~m}^{3}$ is operated in cell recycle mode. At a volumetric flow rate of $10 \mathrm{~m}^{3}$ day ${ }^{-1}$ and effluent bio...