Kinetics Model for Batch Culture of White Rot Fungus
白腐真菌批式发酵动力学模型研究

In order to understand ligninolytic enzymes production process during culture of white rot fungus, accordingly to direct the design of fermentation process, a kinetics model was built for the batch culture of Phanerochaete chrysosporium. The parameters in the model were calibrated based on the experimental data from free and immobilized culture separately. The difference between each variable's values calculated based on kinetics model and experimental data is within 15%. Comparing parameters for the free and the immobilized culture, it is found that maximum biomass concentrations are both 1.78 g/L; growth rate ratio of immobilized culture (0.668 3 d-1) is larger than that of free culture (0.514 4 d-1); very little glucose is consumed for biomass growth in free culture while in immobilized culture much glucose is used and ammonium nitrogen is consumed at a greater rate. ligninolytic enzymes production process is non-growth related; fungal pellets can produce MnP (231 U/L) in free culture with a production rate of 115.8 U·(g·d)-1 before peak and 26.1 U·(g·d)-1 after peak, thus fed-batch is a possible mode to improve MnP production and fermentation efficiency. MnP (410 U/L) and LiP (721 U/L) can be produced in immobilized culture, but MnP and LiP production rate decrease from 80.1 U·(g·d)-1 and 248.9 U·(g·d)-1 to 6.04 U·(g·d)-1 and 0 U·(g·d)-1, respectively, indicating a proper feed moment is before the enzymes peak during fed-batch culture.