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Design and operation of immobilized enzyme reactors

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Advances in Biochemical Engineering, Volume 10

Part of the book series: Advances in Biochemical Engineering ((ABE,volume 10))

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 sρ)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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