Analysis of a continuous, aerobic, fixed-film bioreactor. I. Steady-state behavior.

Abstract:

:The analysis of a continuous, aerobic, fixed-film bioreactor is performed by simulating the behavior of penicillin production in a three-phase fluidized bed. Rigorous mathematical models are developed for a fluidized-bed fermentor in which bioparticles are fluidized by the liquid medium and air. The steady-state performance of the fluidized-bed reactor is appraised in terms of penicillin productivity and outlet concentration by considering the two extremes in contacting patterns, complete back-mix and plug flow, in the absence of a growing biofilm. The results show that the complete back-mix contacting pattern is preferred over that of plug flow due to the nature of the penicillin kinetic relationships. It is also shown that for the dual-nutrient (glucose and oxygen) penicillin reaction system the optimum biofilm thickness does not equal the penetration depth of a limiting nutrient, but depends upon the total reactor configuration.

journal_name

Biotechnol Bioeng

authors

Park Y,Davis ME,Wallis DA

doi

10.1002/bit.260260509

subject

Has Abstract

pub_date

1984-05-01 00:00:00

pages

457-67

issue

5

eissn

0006-3592

issn

1097-0290

journal_volume

26

pub_type

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