Modelling effects of micromixing on performance of continuous bioreactors

机译：微混凝材料对连续生物反应器性能的建模效果

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Effects of micromixing on performance of continuous bioreactors is investigated by determination of upper and lower boundary of substrate conversion. The bounds are evaluated on the basis of limiting micromixing dynamics, i.e. as completely segregated flow and as maximum mixidness flow. Applied is probability density function of residence time (RTD) corresponding to "tank in series" model. Numerical evaluation of the bounds is obtained by solving a set of nonlinear differential equations with asymptotic split boundary conditions. The dependence of the bounds in substrate conversion as functions on the Damkohler number is graphically presented.

机译：通过测定基材转化的上下边界来研究微混凝器对连续生物反应器性能的影响。基于限制微混凝动力学，即完全隔离流动和最大混合流量来评估界限。应用是对应于“串联”模型的停留时间（RTD）的概率密度函数。通过求解具有渐近分裂边界条件的一组非线性微分方程来获得界限的数值评估。图形呈现了基板转换中的边界的依赖性。图形地呈现了Damkohler号上的函数。

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《International Conference on Information Technology Interfaces》|2001年||共6页
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作者
Zelimir Kurtanjek;
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中图分类 G20-53;
关键词
Residence time distribution; Chemostat; Micromixing;

机译：停留时间分布;化学箱;微混合;

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Modelling effects of micromixing on performance of continuous bioreactors

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