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乳链菌肽发酵的主要影响因子
引用本文:庄绪亮,张洪勋,马桂荣,孔健.乳链菌肽发酵的主要影响因子[J].过程工程学报,2000,21(1):93-97.
作者姓名:庄绪亮  张洪勋  马桂荣  孔健
作者单位:1. 中国科学院生态环境研究中心,北京100085
2. 山东大学微生物技术国家重点实验室,济南250100
摘    要:采用中心组合实验设计方法(CentralCompositeDesign),运用SAS统计分析软件,得到了乳链菌肽发酵单位与主要影响因子之间的回归方程:YIU=1087.17+62.86X1+76.18X2+55.41X4-23.35X11.62X-15.67X2X4.根据方程及其岭岭分析结果,设计出含氮量较低的培养基SYS3.同CM培养基相比,原料成本相差不大,但发酵单位提高了64%.同MRS培养基相比,虽然氮源含量降低了约50%;发酵水平却相当,同时发酵液中残留的杂蛋白减少可以降低杂蛋白对Nisin提取的干扰作用.

关 键 词:乳链菌肽  发酵  中心组合设计  SAS统计分析
修稿时间:1999-01-27

Effect of Major Factors of Fermentation Mediumon Nisin Production
ZHUANG Xu-liang,ZHANG Hong-sun,MA Gui-rong,KONG Jian.Effect of Major Factors of Fermentation Mediumon Nisin Production[J].Chinese Journal of Process Engineering,2000,21(1):93-97.
Authors:ZHUANG Xu-liang  ZHANG Hong-sun  MA Gui-rong  KONG Jian
Abstract:By central composite design and the analysis using the SAS software, a quadraticregression equation on the relationship between nisin yield and its major influencing factorssuCh as soy peptone, yeast powder, sucrose and initial PH was formulated:un = 1087.17 62.86x1 76.18X2 55.41X4 - 23.35X2 11.62X-15.67X2X4A medium SYS3 with less nitrogen (soy peptome 6.25 g/L, yeast powder 5 g/L, sucrose 20 g/Land initial PH 7.0) was proposed according to the above equation and bridge analysis. Underthe same production cost, nisin production in the SYS3 medium was increased by 64% ascompared to that in the CM medium and was as same as that in MRS medium. The additionaladvantage is expected for nisin purtification due to the reduction of nitrogen cobment by 50%as compared to the MRS medium.
Keywords:nisin  fermentation  central composite design  SAS statistics analysis
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