首页> 外文期刊>Biochemical Engineering Journal >Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512 (f)
【24h】

Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512 (f)

机译:使用肠膜上亮光乳清蛋白NRRL B512从蔗糖生产右旋糖酐酶,右旋糖酐和果糖(f)

获取原文
获取原文并翻译 | 示例
           

摘要

The production of dextransucrase, dextran and fructose by surose fermentation using Leuconostoc mesenteroides NRRL-B152(F) was studied in batch operation in a bioreactor with total volume of 1.5 dm~3. The effect of temperature (20 to 40 deg C), pH (5.5 AND 6.7) and sucorse concentration (10 to 120 g/l) on process performance was studied. The optimum conditions for dextran and fructose production were T = 35 deg C and pH = 5.5. Cell growth is inhibited by high sucrose concentrations: however, for sucrose concentration higher than 40 g/dm~3 separation of products from cells is difficult. Biomass (X), enzyme (E), dextran (D), fructose (F) and sucrose (S) rate equations were considered in order to derive a simple fermentation kinetic model from batch experimental data. The logistic equation provided a reasonable description for cell concenctration. X. The Luedeking and Piret equation was used to describe the enzyme production rate, by considering only the growth associated term. The concentrations of products (dextran and frutose) were reasonably described by a first order kinetic law with respect to both substrate and enzyme concentrations; the substrate, S was consumel for cell growth and for dextran and fructose production. Model parameters #mu#_m and X_o were calculated from cell growth as a function of time. The yield Y_(E/X) were calculated from X_(max) and E_(max) and Y_(X/S) was estimated from X_(max) and the sucrose consumed by the bacteria. The remaining parameter k' was obtained by fitting the experimental data of substrate, dextran and fructose concentrations versus time.
机译:在总体积为1.5 dm〜3的生物反应器中分批操作研究了使用Mesenteroides NRRL-B152(F)进行蔗糖发酵进行蔗糖发酵生产葡聚糖酶,葡聚糖和果糖。研究了温度(20至40摄氏度),pH(5.5和6.7)和蔗糖浓度(10至120克/升)对工艺性能的影响。葡聚糖和果糖生产的最佳条件是T = 35℃和pH = 5.5。蔗糖浓度高会抑制细胞生长:但是,当蔗糖浓度高于40 g / dm〜3时,很难从细胞中分离出产物。为了从批处理实验数据中得出简单的发酵动力学模型,考虑了生物质(X),酶(E),右旋糖酐(D),果糖(F)和蔗糖(S)速率方程。逻辑方程为细胞浓缩提供了合理的描述。 X.通过仅考虑生长相关项,使用Luedeking和Piret方程描述酶的产生速率。通过一阶动力学定律,就底物和酶的浓度合理地描述了产物(右旋糖酐和果糖)的浓度。在底物上,S消耗细胞生长以及葡聚糖和果糖生产。从细胞生长随时间计算模型参数#mu#_m和X_o。由X_(max)和E_(max)计算产率Y_(E / X),并由X_(max)和细菌消耗的蔗糖估算Y_(X / S)。通过拟合底物,葡聚糖和果糖浓度相对于时间的实验数据获得剩余参数k'。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号