Abstract:
:Oxygen uptake rate and oxygen mass transfer rate have been studied during xanthan gum production process in stirred tank bioreactor. Empirical equations for the oxygen mass transfer coefficient have been obtained taking into account several variables such as air flow rate, stirrer speed and apparent viscosity. Oxygen uptake rate evolution in the course fermentation has been measured, obtaining an equation as a function of biomass concentration, including overall growth and non growth-associated oxygen uptake. A metabolic kinetic model has been employed for xanthan gum production description including oxygen mass transfer and uptake rates. The results point out that this model is able to describe adequately not only oxygen dissolved evolution, but also of the production of xanthan and substrate consumption. Also, the influence of several parameters (k(L)a, air flow rate and dissolved oxygen) in the evolution of the key compounds of the system have been studied. The results of the simulation shown that an increasing of dissolved oxygen concentration favor the xanthan gum production.
journal_name
Enzyme Microb Technoljournal_title
Enzyme and microbial technologyauthors
García-Ochoa F,Castro EG,Santos VEdoi
10.1016/s0141-0229(00)00272-6keywords:
subject
Has Abstractpub_date
2000-11-15 00:00:00pages
680-690issue
9eissn
0141-0229issn
1879-0909pii
S0141022900002726journal_volume
27pub_type
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