Theory for Continuous Cultivation

The theory for microbial processing starts with the concept of growth-limiting nutrient. Use "BACK" to return to here if you stop for review.

There are several mathematical relationships of specific growth rate coefficient to concentration of growth-limiting nutrient, but the Monod equation is by far the most popular. The Monod equation is:

Well-mixed continuous processes

  • Elementary treatment of background concepts

    We will first study a process with such good mixing that all fluid elements are assumed to be identical. The analysis starts with the mass balance equation:

    rate of change = input - output ± reaction

    V dx/dt = 0 + µ x V - F x

  • where x = organism concentration in g/L at time t
  • V =the constant volume of the vessel
  • F = feed rate
  • µ = specific growth rate coefficient
  • xo organism concentration in the feed

    If we neglect organisms in the feed stream, the F xo term is not needed. With aseptic operation, the feed is sterile.

    Because all fluid elements are assumed to be identical, x in the vessel is the same as x in the overflow. A new term D, the dilution rate, is equal to F/V, thus dividing each term in the equation by V and dropping the zero term gives

    µ x = D x

  • Click here if this transformation was not obvious.

    A mass balance for the nutrient in lowest proportions for growth the growth-limiting nutrient (same link as above) ) gives:

    where:

  • M = maintenance coefficient for endogenous metabolism
  • Y = yield coefficient, mass of cells per mass of nutrient consumed

    Again the equation would benefit from dividing every term by V and substituting D for F/V. An equation is needed to relate µ to S, and we can use the Monod equation or one of the various inhibition equations.

    At steady state, there is no change thus the derivatives in the differential equations disappear so that µ = D and

    Substituting D for µ in the Monod Equation and solving for S gives:

    Solving for x after substituting D for µ gives:

    This is an old, familiar analysis for any continuous culture that meets the assumptions of perfect mixing, no organisms in the feed, and constant volume. The equations are fundamental except for the Monod equation that has no time dependency and should be applied with caution to transient states where there may be a time lag as µ responds to changing S.


    There is a computer exercise that draws µ versus S as you specify the coefficients, but the links are not ready.
  • Limitations other than the carbonaceous nutrient

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    (c) 1995 H. Bungay