| 白腐真菌批式发酵动力学模型研究 |
| 摘要点击 2369 全文点击 2759 投稿时间：2007-03-19 修订日期：2007-05-04 |
| 查看HTML全文
查看全文 查看/发表评论 下载PDF阅读器 |
| 中文关键词 黄孢原毛平革菌 木质素降解酶 动力学模型 批式发酵 |
| 英文关键词 Phanerochaete chrysosporium ligninolytic enzymes kinetics model batch culture |
|
| 中文摘要 |
| 为了进一步认识白腐真菌发酵产酶机理并指导相关发酵工艺设计，在一系列试验研究的基础上，建立了描述黄孢原毛平革菌批式发酵过程的动力学模型，并采用自由悬浮和固定化2种培养条件下的试验数据分别回归了模型各参数.模拟计算结果表明，生物量、葡萄糖、氨氮、木质素酶浓度的的计算值与实测值的偏差在15%以内.对比2种培养条件下的模型参数发现，二者得到的最大生物量浓度均为1.78 g/L；固定化培养菌体的比增长速率值（0.668 3 d-1）大于自由悬浮培养值（0.514 4 d-1）；自由悬浮培养中绝大部分葡萄糖消耗于非生长菌体代谢，固定化培养中则部分葡萄糖用于菌体生长，且氨氮消耗更快；菌体的产酶过程与生长无关；自由悬浮培养条件下，菌丝小球可合成MnP（231 U/L），其MnP合成能力为115.8 U·(g·d)-1，且高峰后依然可以保持26.1 U·(g·d)-1，适合采用补料-分批发酵的模式提高MnP的产量及其发酵效率；固定化培养条件下，菌体可同时合成MnP（410 U/L）和 LiP（721 U/L），但其LiP和MnP合成能力在酶活高峰之后明显下降，分别由248.9 U·(g·d)-1和80.1 U·(g·d)-1下降到0 U·(g·d)-1和6.04 U·(g·d)-1，故而在考虑补料-分批发酵模式时，补料时机应选择在培养中期的LiP与MnP峰值之前. |
| 英文摘要 |
| 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. |
