Multiphase Bioreactor Design

line corresponds); b) dissolved oxygen concentration profiles. OPERATION AND APPLICATIONS OF FLOCCULATION BIOREACTORS As well as ...

Figure 13.6 Hocculation bioreactor response to increasing dilution rate (D) with a feed lactose concentration of 57.2 g.L − 1 ; ...

parameters of the same flocculent strain of S. cerevisiae during the startup of a continuous fermentation. A strong influence of ...

Figure 13.7 a) Comparison between specific rates of glucose consumption and ethanol production obtained with the original system ...

ethanol productivity obtained with the original system () and the modified system vs. dilution rate. are widely used. However, ...

the dairy industry produced in large amounts, but also allowing for the production of a useful fuel. There is the need for more ...

airlift extract 1995 Z. mobilis+ Saccharomyces sp. agitated conical flasks 1 — ethanol 1.5 Abate et al. 1996 Rhodiola sachalinen ...

Freitas, C. and Teixeira J.A. (1997) Hydrodynamic Studies in an Airlift Reactor with and Enlarged Degassing Zone. Bioprocess Eng ...

Lu, W.-J., Hwang, S.-J. and Chang, C.-M. (1995) Liquid Velocity and Gas Holdup in Three-Phase Internal Loop Airlift Reactors wit ...

Siegel, M.H., Hallaile, M., Herskowitz, M. and Merchuk, J.C. (1988) Hydrodynamics and Mass Transfer in a Three-Phase Airlift Rea ...

Teixeira, J.A. and Mota, M. (1990) Experimental Assessment of Internal Diffusion Limitations in Yeast Flocs. Chem. Eng. J., 43, ...

...

CHAPTER FOURTEEN BIOREACTOR DESIGN FOR PLANT CELL SUSPENSION CULTURES PATRICIA M.KIERAN Department of Chemical Engineering, Univ ...

al., 1997). Table 14.1 summarises current commercial/near commercial processes involving plant cell suspensions. From an enginee ...

Table 14.1 Commerical/near-commercial processes involving plant cell suspension cultures Product (system) Application Company Sc ...

Table 14.2 Other examples of (non-commercial) large-scale (>500 L) systems System Company Scale/Operating Details Reference A ...

1: <100 high Figure 14.1 Micrographs of (a) M. citrifolia and (b) D. capensis cells in Bioreactor design for plant cell suspe ...

suspension culture, cultivated in shake flasks (Bar represents 50 μm). (a) Morinda ctirifolia and (b) Drosera capensis cells, cu ...

Many studies have focused on the identification of optimal aggregate size distributions for metabolite production (e.g. Hulst et ...

Emery, 1993). For comparison purposes, apparent viscosity values for the non- Newtonian M. citrifolia broth have been calculated ...