General hybrid multizonal/CFD approach for bioreactor modeling
暂无分享,去创建一个
Sandro Macchietto | Fabrizio Bezzo | Constantinos C. Pantelides | S. Macchietto | F. Bezzo | C. Pantelides
[1] F. García-Ochoa,et al. Mass transfer coefficient in stirred tank reactors for xanthan gum solutions , 1998 .
[2] W. Schmidell,et al. Volumetric oxygen transfer coefficients (kLa) in batch cultivations involving non-Newtonian broths , 2001 .
[3] Doraiswami Ramkrishna,et al. On the solution of statistical models of cell populations , 1971 .
[4] E. Papoutsakis,et al. Fluid-mechanical damage of animal cells in bioreactors. , 1991, Trends in biotechnology.
[5] Sandro Macchietto,et al. A general framework for the integration of computational fluid dynamics and process simulation , 2000 .
[6] Dardo Marqués,et al. Optimal control of a batch bioreactor for the production of xanthan gum , 2001 .
[7] Sandro Macchietto,et al. Model based control of a multipurpose batch reactor - an experimental study , 1995 .
[8] G. Eigenberger,et al. Multiscale modeling of hydrodynamics, mass transfer and reaction in bubble column reactors , 2001 .
[9] D. Cooper,et al. Development and solution of a cell mass population balance model applied to the SCF process , 1999 .
[10] D. Kyriakidis,et al. Kinetics of xanthan gum production from whey by constructed strains of Xanthomonas campestris in batch fermentations , 1997 .
[11] Costas Kiparissides,et al. Prediction of particle size distribution in suspension polymerization reactors: effect of turbulence nonhomogeneity , 2000 .
[12] Prodromos Daoutidis,et al. Numerical solution of a mass structured cell population balance model in an environment of changing substrate concentration , 1999 .
[13] C. Hewitt,et al. Studies related to the scale-up of high-cell-density E. coli fed-batch fermentations using multiparameter flow cytometry: effect of a changing microenvironment with respect to glucose and dissolved oxygen concentration. , 2000, Biotechnology and bioengineering.
[14] Matthias Bauer,et al. A concept for multi-scale modeling of bubble columns and loop reactors , 1999 .
[15] Alvin W. Nienow,et al. Mixing: Studies at the University of Birmingham on This Traditional Technology Critical in the Manufacture of New Biological Products , 2000 .
[16] Mohsen H. Al-Rashed,et al. CFD modelling of gas–liquid reactive precipitation , 1999 .
[17] A. Schumpe,et al. The influence of agitation rate on xanthan production by Xanthomonas campestris. , 1989, Biotechnology and bioengineering.
[18] F. García-Ochoa,et al. Metabolic structured kinetic model for xanthan production , 1998 .
[19] D. Ollis,et al. Extracellular microbial polysaccharides. II. Evolution of broth Power‐law parameters for xanthan and pullulan batch fermentation , 1980 .
[20] H. Wei,et al. Application of CFD Modelling to Precipitation Systems , 1997 .
[21] Fabrizio Bezzo. Design of a General Architecture for the integration of Process Engineering Simulation and Computational Fluid Dynamics , 2001 .
[22] Zhiming Zheng,et al. EFFECT OF FLUID RHEOLOGICAL PROPERTIES ON MASS-TRANSFER IN A BIOREACTOR , 1995 .
[23] C. Hewitt,et al. Physiological responses to mixing in large scale bioreactors. , 2001, Journal of biotechnology.
[24] A. B. Metzner. Agitation of non‐Newtonian fluids , 1957 .
[25] Jerzy Bałdyga,et al. Barium sulphate precipitation in a pipe — an experimental study and CFD modelling , 2001 .
[26] B. Mayr,et al. Simulation of the effect of mixing, scale-up and pH-value regulation during glutamic acid fermentation , 1995 .
[27] Serafim D. Vlaev,et al. Macro-Mixing and Streptomyces fradiae: Modelling Oxygen and Nutrient Segregation in an Industrial Bioreactor , 2000 .
[28] C. Dussap,et al. Modelling Xanthomonas campestris batch fermentations in a bubble column , 1989, Biotechnology and bioengineering.
[29] F. García-Ochoa,et al. Xanthan gum production: An unstructured kinetic model , 1995 .
[30] David F. Ollis,et al. Biochemical Engineering Fundamentals , 1976 .
[31] E. Galindo,et al. Prediction of xanthan fermentation development by a model linking kinetics, power drawn and mixing , 1998 .
[32] Michael A. Henson,et al. Model predictive control of continuous yeast bioreactors using cell population balance models , 2000 .
[33] F. García-Ochoa,et al. Oxygen transfer and uptake rates during xanthan gum production. , 2000, Enzyme and microbial technology.
[34] Costas Kiparissides,et al. Use of CFD in prediction of particle size distribution in suspension polymer reactors , 1998 .
[35] Götz Lauschke,et al. CFD in der chemischen Verfahrenstechnik aus industrieller Sicht , 2000 .
[36] H. Kramer,et al. Design of industrial crystallisers for a given product quality , 1999 .