Abstract
A short review of the research in the past two years (1990–1991) on immobilized whole cells, such as microbial, plant, and animal cells, is presented including a discussion from an engineering point of view. Recent works concerning the intraparticle mass transfer effect on immobilized microbial cells by the authors and their co-workers are also introduced. Finally, future prospects of the immobilized cell system will be discussed.
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Abbreviations
- Dep :
-
effective diffusivity of ethanol inside the gel particles [m2 h−1]
- Des :
-
effective diffusivity of glucose inside the gel particles [m2 h−1]
- D0p :
-
diffusivity of ethanol in water [m2 h−1]
- D0s :
-
diffusivity of glucose in water [m2 h−1]
- Ip(P):
-
product inhibition function for cell growth [-]
- I′p(P):
-
product inhibition function for ethanol production [-]
- Is(S):
-
substrate inhibition function for cell growth [-]
- I′s(S):
-
substrate inhibition function for ethanol production [-]
- Ki :
-
substrate inhibition constant for ethanol production [g l−1]
- Kp :
-
product inhibition constant for cell growth [g l−1]
- K′p :
-
product inhibition constant for ethanol production [g l−1]
- Ks :
-
substrate limitation constant for cell growth [g l−1]
- K′s :
-
substrate limitation constant for ethanol production [g l−1]
- k1 :
-
constant in the diffusivity relation [-]
- k2 :
-
constant in the diffusivity relation [l g−1]
- P:
-
product (ethanol) concentration [g l−1]
- Pmax :
-
maximum product concentration for cell growth [g l−1]
- P′max :
-
maximum product concentration for ethanol production [g l−1]
- Pi :
-
transition concentration for product inhibition for cell growth [g l−1]
- P′i :
-
transition concentration for product inhibition for ethanol production [g l−1]
- r:
-
distance from the center of particles [m]
- rp :
-
specific production rate [g EtOH per g dry cell per h]
- rp0 :
-
specific production rate without product inhibition [g EtOH per g dry cell per h]
- rpm :
-
maximum specific production rate [g EtOH per g dry cell per h]
- rs :
-
production rate per unit surface area of cell-immobilizing particles [g EtOH per mm2 per h]
- R:
-
radius of immobilized particle [m]
- S:
-
substrate (glucose) concentration [g l−1]
- Smax :
-
maximum substrate concentration [g l−1]
- Si :
-
threshold concentration for substrate inhibition [g l−1]
- S0 :
-
substrate concentration in the bulk solution [g l−1]
- t:
-
time [h]
- X:
-
cell concentration [g dry cell per l]
- X0 :
-
initial cell concentration [g dry cell per l]
- Yp/s :
-
yield of ethanol from glucose [g EtOH per g glucose]
- μ:
-
specific growth rate [h−1]
- μ0 :
-
specific growth rate without product inhibition [h−1]
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Furusaki, S., Seki, M. (1992). Use and engineering aspects of immobilized cells in biotechnology. In: Modern Biochemical Engineering. Advances in Biochemical Engineering/Biotechnology, vol 46. Springer, Berlin, Heidelberg. https://doi.org/10.1007/BFb0000710
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DOI: https://doi.org/10.1007/BFb0000710
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