| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 35850 | Process Biochemistry | 2008 | 6 Pages |
Abstract
Repeated-batch cultures of Ca-alginate immobilized cells of Streptomyces olindensis ICB20 for retamycin production were carried out in two different bioreactors: a basket-type stirred tank reactor (BSTR) and a bubble column reactor (BCR). Higher average values of retamycin content (R) and productivity (PR) were achieved in the BSTR cultures (about 1.7 AU and 0.031 AU h−1, respectively) compared to those obtained in the BCR cultures (about 0.6 AU and 0.012 AU h−1, respectively). The BCR, on the other hand, presented significantly better operation stability than the BSTR, which makes the former much more promising regarding future industrial applications.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Bioengineering
Authors
Iara Rebouças Pinheiro, Maria Cândida Reginato Facciotti,
