Bioreactor washout dilution rate

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SUMMARY

The discussion centers on calculating the dilution rate at which washout occurs in a Continuous Stirred Tank Reactor (CSTR) for a product P produced from gram-negative bacteria, following the Monod growth law. Key parameters include a maximum growth rate (μmax) of 1 hr-1, a half-saturation constant (KM) of 0.25 g/L, and a yield coefficient (YC/S) of 0.5 g/g. The user expresses confusion regarding the relationship between the rates of substrate consumption (rS), cell production (rC), and cell generation (rg), ultimately clarifying that rg and rC are equivalent under the assumption of negligible cell death.

PREREQUISITES
  • Understanding of Monod growth kinetics
  • Familiarity with Continuous Stirred Tank Reactor (CSTR) operations
  • Knowledge of mass balance equations in bioprocessing
  • Basic concepts of microbial growth and substrate utilization
NEXT STEPS
  • Study Monod growth kinetics in detail
  • Learn how to perform mass balance calculations in bioreactors
  • Explore the differences between various rates in bioprocessing (rS, rC, rg)
  • Investigate the impact of dilution rates on microbial growth in CSTRs
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Students and professionals in biochemical engineering, microbiology, and bioprocessing who are involved in reactor design and optimization, particularly those focusing on continuous fermentation processes.

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Homework Statement


The production of a product P from a particular gram negative bacteria follows the Monod growth law
$$-r_{S} = \frac {\mu_{max}C_{S}C_{C}}{K_{M}+C_{S}}$$
with ##\mu_{max} = 1 \hspace{0.05 in} hr^{-1}##, ##K_{M} = 0.25 \hspace{0.05 in} g/L##, and ##Y_{C/S} = 0.5 \hspace{0.05 in} g/g##

The reaction is now to be carried out in a CSTR with ##C_{S0}## = 20 g/L and ##C_{C0}## = 0 g/L. What is the dilution rate at which washout occurs?

Homework Equations

The Attempt at a Solution


I do a mass balance on the cell being produced
$$V \frac {dC_{C}}{dt} = -\nu C_{S} + (r_{g} - r_{d})V $$
Assume the death rate is negligible
$$ \frac {dC_{C}}{dt} = -DC_{S} + r_{g} $$
Assume steady state
$$ DC_{S} = r_{g} $$
Now this is where I run into a problem. I am not sure how how to express ##r_{g}##. I get confused because 3 different variables are used, ##r_{S}##, ##r_{C}##, and ##r_{g}## in these bioreactor problems. I know S is the substrate and C is cells, but what is g? Is g and C the same thing? Anyways, I thought ##r_{g} = -r_{S}##, but it turns out from the solution manual that ##r_{g} = -Y_{C/S}r_{S}##, but I thought that ##r_{C} = -Y_{C/S}r_{S}##.

This is part (c) in the problem, but part (a) states
The reaction is to be carried out in a batch reactor with the initial cell concentration of ##C_{C0}## = 0.1 g/L and substrate concentration of ##C_{S0}## = 20 g/L
##C_{C} = C_{C0} + Y_{C/S}(C_{S0} - C_{S})##
Plot ##-r_{S}##, ##-r_{C}##, ##C_{S}##, and ##C_{C}##, as a function of time.

I know ##r_{C} = -Y_{C/S}r_{S}##, but I don't know the difference between ##r_{g}## and ##r_{C}##. They use different variables in the same problem, and I am uncertain if they mean the same thing or mean something different.
 
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I think this would be better placed in the Biology, Chemistry & Earth Homework forum. Left to your own devices, a web search for a similar worked example is what you need.

Good luck
 
Just took the final for this class, so it's moot now! but in this case, ##r_{C}## and ##r_{g}## are the same, because ##r_{C} = r_{g} - r_{d}##, where g is cell generation, and d is cell death. We are assuming cell death is negligible.
 

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