Abstract
This review encompasses recent advances in the design and operation of immobilized enzyme reactors for industrial applications. Basic immobilized enzyme reactor engineering concepts are described as a reference point for recent innovations. Although practical examples are cited, the subject is approached from the viewpoint of reactor design and operation and the potential general applicability of new concepts or developments. Areas reviewed include reactor types, reactor performance, operating strategy, and general design and economic considererations. Most of the progress reported in this field is in the form of refinements, rather than basic innovations.
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Abbreviations
- am :
-
surface area per unit volume
- av :
-
ratio of particle surface area to reactor volume
- dp :
-
particle diameter
- D:
-
substrate diffusivity
- Deff :
-
effective diffusivity=DΘ/τ
- D0 :
-
bulk diffusivity
- E:
-
enzyme activity
- Et :
-
total enzyme activity
- F:
-
flow rate
- Fi :
-
initial feed rate
- g:
-
acceleration due to gravity
- G:
-
mass velocity per unit superficial bed cross section
- H:
-
number of half-lives utilization of IME
- J:
-
dimensionless group
- k:
-
turnover number
- km :
-
mass transfer coefficient
- k'm :
-
value of km for a sphere setting at its terminal velocity
- kv :
-
reaction velocity constant
- K:
-
equilibrium constant
- Ki :
-
product inhibition constant
- Km :
-
Michaelis constant
- K'm :
-
substrate inhibition constant
- Kp :
-
constant (Michaelis type for reverse reaction)
- L:
-
flat plate thickness
- Lc :
-
bed height
- m:
-
order of reaction
- M:
-
general modulus
- N:
-
number of reactors
- NGa :
-
Galileo number=d 3p ρ(ρ s − ρ)g/u2
- NPe :
-
Peclet number=dpu/D
- NRe :
-
Reynolds number=dpG/μ
- (NRe)mf :
-
minimum fluidization Reynolds number
- NSc :
-
Schmidt number=μ/ρD
- P:
-
product concentration
- Pt :
-
total production
- r:
-
radial distance
- Rp :
-
ratio of low to high production rate
- S:
-
substrate concentration
- Sb :
-
bulk substrate concentration
- S0 :
-
initial substrate concentration
- Ss :
-
substrate concentration at catalyst surface
- St :
-
total substrate concentration if all product coverted to substrate
- t:
-
reaction time
- t1/2 :
-
enzyme half life
- tp :
-
total period of time of reactor operation
- u:
-
fluid velocity
- v:
-
reaction velocity
- vi :
-
intrinsic reaction rate
- Vm :
-
kE (maximum reaction velocity)
- Vs :
-
substrate volume
- W:
-
weight of immobilized enzyme
- X:
-
(S0 − S)/S0=fractional conversion
- Xe :
-
Xt at equilibrium
- Xi :
-
St − S0/St
- Xt :
-
St − S/St
- Y1 :
-
mole fraction substrate in feed
- Y2 :
-
mole fraction substrate in product
- z:
-
column height, assuming film diffusion to the rate controlling step
- Z:
-
(NRe)mf/RRe
- ε:
-
void fraction
- η:
-
effectiveness factor
- OL:
-
modulus
- μ:
-
fluid viscosity
- ρ:
-
fluid density
- ρ s :
-
solid density
- Θ:
-
particle internal porosity
- τ:
-
tortuosity (ratio of actual diffusion path length to straight line distance)
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Pitcher, W.H. (1978). Design and operation of immobilized enzyme reactors. In: Advances in Biochemical Engineering, Volume 10. Advances in Biochemical Engineering, vol 10. Springer, Berlin, Heidelberg. https://doi.org/10.1007/BFb0004469
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DOI: https://doi.org/10.1007/BFb0004469
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