Effects of fed-batch and continuous fermentations on human lysozyme production by Kluyveromyces lactis K7 in biofilm reactors

被引:0
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作者
Duygu Ercan
Ali Demirci
机构
[1] The Pennsylvania State University,Department of Agricultural and Biological Engineering
[2] The Pennsylvania State University,The Huck Institutes of Life Sciences
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Human lysozyme; Fed-batch; Continuous; Suspended cell reactor; Biofilm reactor; Plastic composite support;
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摘要
Lysozyme is a lytic enzyme, which has antimicrobial activity. It has been used for food and pharmaceutical applications. This study was undertaken to evaluate fed-batch and continuous fermentations for the human lysozyme production in biofilm reactor. Results showed that addition of lactose the mid-log phase to make the concentration back to the initial level generates higher lysozyme production (177 U/ml) compared with lactose addition in late-log phase (174 U/ml) (p < 0.05). Moreover, fed-batch fermentation with glucose as initial carbon source and continuous addition of lactose with 0.6 ml/min for 10 h demonstrated significantly higher lysozyme production (187 U/ml) compared to the batch fermentation (173 U/ml) (p < 0.05). In continuous fermentation, biofilm reactor provided significantly higher productivity (7.5 U/ml/h) compared to the maximum productivity in suspended cell bioreactor (4 U/ml/h), because the biofilm reactor provided higher cell density at higher dilution rate compared to suspended cell reactor (p < 0.05).
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页码:2461 / 2468
页数:7
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