Multiphase Bioreactor Design
Both hypotheses require enzyme to be retained in the pores of the membrane. In each series of reactors there is a distribution o ...
Figure 7.9 Representation of different models and their correlation to the experimental results. (From Carvalho et al., 2001b) A ...
The velocity on the surface of the membrane is 10^5 times higher than inside the membrane pores. These velocities have quite dif ...
[E] overall enzyme concentration (ML−^3 ) εm porosity (dimensionless) σobs observed solute rejection (dimensionless) [Prot]p con ...
Protmemb protein interacting with the membrane (M) Protp protein in the permeate (M) Protr protein in the retentate (M) Pv volum ...
degree in the permeate stream (dimensionless) Xf conversion degree at final time (dimensionless) Xi conversion degree at initial ...
Carvalho, C.M.L., Aires-Barros, M.R. and Cabral, J.M.S. (2000b) Performance of a membrane reactor for enzymatic transesterificat ...
Gajjar, L., Singh, A., Dubey, R.S. and Srivastava, R.C. (1997) Enzymatic activity of whole cells entrapped in reversed micelles. ...
Holmberg, K. (1998) Quarter century progress and new horizons in microemulsions. In: Micelles, microemulsions and monolayers: sc ...
Levenspiel, O. (1972) Chemical Reaction Engineering, John Wiley & Sons, New York. Luisi, P.L. (1985) Enzymes hosted in rever ...
Patel, M.T., Nagarajan, R. and Kilara, A. (1996a) Lipase-catalysed biochemical reactions in novel media: a review. Chem. Eng. Co ...
Verhaert, R.M.D., Hilhorst, R., Vermuë, M., Schaafsma, T. and Veeger, C. (1990) Description of enzyme kinetics in reversed micel ...
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CHAPTER EIGHT SOLID-TO-SOLID BIOCONVERSIONS: BATCH OR CONTINUOUS? M.J.F.MICHIELSEN, RENE H.WIJFFELS, JOHANNES TRAMPER AND H.H.BE ...
For extraction of hydrophilic substrates and/or products, like proteins, a second aqueous phase may be suitable (Hustedt et al., ...
The majority of studies on solid-to-solid bioconversions have been executed in batch systems. From these studies, we first deriv ...
Classification The classification of batch solid-to-solid bioconversions shown in Figure 8.1 is based on the preparation of each ...
TE is the eutectic temperature (adapted from Gill and Vulfson, 1994). In order to make an appropriate choice, if possible, betwe ...
synthesis of sugar fatty acids 34–100 0.5.10−^3 – 5.0.10−^3 Cao et al. (1996) 3 peptide synthesis 56–97 0.5–10–4–2.7 Eichhorn et ...
particles to the reactor wall. Vibrating the whole reactor could not elucidate this. This indicates that further improvements of ...
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