semi-quantitative modeling for the effect of oxygen level.pdf
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7/27/2019 Semi-quantitative Modeling for the Effect of Oxygen Level.pdf
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Semi-quantitative Modeling for the Effect of Oxygen Level
on the Metabolism inEscherichia coli
Yu Matsuoka1, Kazuyuki Shimizu1,21Dept. of Bioscience and Bioinformatics, Kyushu Institute of Technology,
Iizuka, Fukuoka 820-8502, Japan2Institute for Advanced Biosciences, Keio University, Tsuruoka, Yamagata 997-0017, Japan
E-mail: [email protected]
Abstract
Mathematical models for the main metabolic
pathways such as glycolysis, pentose phosphate
pathway, TCA cycle, fermentation pathway etc. were
considered for the enzyme level regulation in E.coli. Itis quite important to develop a model which can
simulate the effect of oxygen level on the metabolism in
practice. For this, the effect of oxygen level on the
expressions of the global regulators such as arcA/B
and fnr was modeled based on the experimental data.
Then the effects of these gene expressions on the
metabolic pathway gene expressions were
incorporated in the model, where the effects of oxygen
levels on PDHc and Pfl fluxes as well as the
respiratory pathway flux were expressed based on the
experimental data. Thus, the model could express the
increase in the redox ratio, NADH/NAD as the oxygen
level decreases, and in turn the activation of the
fermentation pathways. The semi-quantitative modeldeveloped in the present research enables us to
simulate the effect of changing the oxygen level on the
cell growth and the production of the variety of
metabolites such as lactate, ethanol etc.
1. Introduction
One of the most challenging goals of metabolic
engineering and bioprocess engineering is to design the
cell metabolism based on metabolic regulation analysis
and to find the optimal culture condition for the cell
growth and the specific metabolite production. For this,
it is strongly desired to develop a mathematical model
which can describe the dynamic behavior of the cell
metabolism in response to culture environment and/or
genetic modifications.
Some of the kinetic models have been developed in
the past for Saccharomyces cerevisiae [1-3]. The
dynamics of the intracellular metabolite concentrations
in response to the pulse addition of glucose-limited
continuous culture have been investigated [2, 4-6].
The kinetic equations for the glycolysis and pentose
phosphate (PP) pathway in E.coli have also beendeveloped by Chassagnole et al. [7] to simulate the
dynamics of the intracellular metabolite concentrations
in response to the pulse change in the feed glucose
concentration in glucose-limited continuous culture.
This model does not contain kinetic equations for the
TCA cycle as well as fermentation pathways, and thus
cannot simulate the typical batch cultivation.
In the present investigation, we considered the
kinetic model equations for the glycolysis, PP
pathweay, TCA cycle and the fermentation pathways.
Moreover, most of the kinetic models developed so far
can express only enzyme level regulation due to the
change in the concentrations of substrate, product aswell as various effectors. Thus, the conventional model
cannot express the metabolic changes in relation to the
change in culture environment such as dissolved
oxygen and/or the genetic changes, where those affect
the cell metabolism via gene level regulation. Although
it is not easy to express gene level regulation by
mathematical equations, we considered a semi-
quantitative approach by utilizing some of the
experimental data and the knowledge on gene level
regulation.
2. Modeling
2.1. Dynamic Equations
Referring to Fig.1, the dynamic equations may be
described based on mass balances as follows:
( ) ][][ XGlcdt
Xd ex=
(1a)
Digital Object Identifier inserted by IEEE
International Conference on Complex, Intelligent and Software Intensive Systems
978-0-7695-3575-3/09 $25.00 2009 IEEE
DOI 10.1109/CISIS.2009.179
215
International Conference on Complex, Intelligent and Software Intensive Systems
978-0-7695-3575-3/09 $25.00 2009 IEEE
DOI 10.1109/CISIS.2009.179
215
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][][
Xvdt
GlcdPTS
ex
=(1b)
]6[]6[
6 PGvvvdt
PGdPDHGPfkPTS =
(1c)
][][
FDPvvdt
FDPdAldPfk =
(1d)
][2
][
GAPvvdt
GAPd
GAPDHAld =
(1e)
][][
PGPvvdt
PGPdPgkGAPDH =
(1f)
]3[]3[
PGvvdt
PGdEnoPgk =
(1g)
][][
PEPvvvvvdt
PEPdPTSPpcPykPckEno +=
(1h)
][][
PYRvvvvvdt
PYRdPflLDHPDHPTSPyk +=
(1i)
][][
LACvdt
LACdLDH =
(1j)
][][
AcCoAvvvvvdt
AcCoAdCSALDHPtaPflPDH +=
(1k)
][
][
AcAldvvdt
AcAlddADHALDH
=(1l)
][][
ETHvdt
ETHdADH =
(1m)
][][
AcPvvdt
AcPdAckPta =
(1n)
]])[[(][
XACEvdt
ACEd exAck
ex
=(1o)
][][
CITvvdt
CITdICDHCS =
(1p)
]2[]2[
2 KGvvdt
KGdKGDHICDH =
(1q)
][][
2SUCvvv
dt
SUCdSDHFrdKGDH
+=(1r)
][
][
FUMvvvdt
FUMdFrdFumSDH
=(1s)
][][
MALvvdt
MALdMDHFum =
(1t)
][][
OAAvvvvdt
OAAdPckCSPpcMDH +=
(1u)
where [.] denotes the concentration. is the specific
growth rate, and iv are the kinetic rate equations in
mmol/gDCW.h.
As shown in Fig.1, G6P and F6P were lumped
together, since Pgi reaction is well in equilibrium. In
the same reason, GAP and DHAP were also lumped
together. A sequence of enzymatic reactions by Gpm,
and Eno may be considered to be in equilibrium, andwas assumed to be one reaction from 3PG to PEP. As
for the PP pathway, only G6PDH and PGDH were
considered in view of NADPH production.
Here, Mez, Icl, MS, Acs, Pps, Fbp etc. were not
considered in the present study, since the focus of the
current attention is fermentation under micro-aerobic
or anaerobic condition.
Fig.1 Metabolic Pathways
2.2.Kinetic equationsSome of the important kinetic equations used for the
various enzyme-catalyzed reactions are as follows:
2.2.1. Cell growth
The specific growth rate was assumed to be the
following simple Monod model:
( )][
][
,
ex
Glcm
ex
mex
GlcK
GlcGlc
ex +
=
(2a)
2.2.2. Phosphotransferase system (PTS)
The glucose transport via phosphotransferase
system (PTS) has been extensively investigated and is
catalyzed by a sequence of enzymes such as EI, HPr,
EIIAGlc and the rate-limiting step to the final step of
glucose transport and phosphorylation from PEP.
Those were encoded by such genes as ptsHI, crr and
ptsG. The kinetic rate equation for PTS may be
expressed as [7]
+
+++
=
PGPTS
n
exexaPTSaPTSaPTS
exPTS
PTS
K
PG
PYR
PEPGlcGlcKPYR
PEPKK
PYR
PEPGlcv
vPGPTS
6,
3,2,1,
max
6,]6[1][
][][][][
][
][
][][
(2b)
Fig.2a shows the effect of [PEP] onPTSv
with respect to
glucose concentration, wherePTSv
increases as [PEP]
increases.
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Fig.2a Effect of [PEP] on PTSv
2.2.3. PhosphofructokinaseThe phosphofructokinase (Pfk) is encoded by pfkA
and pfkB in E.coli, where Pfk-1 encoded by pfkA is
dominant, accounting for 90 % of the total activity [8].
Here, we considered only Pfk-1, where it is inhibited
by PEP [9], and its reaction rate may be expressed as
[7]
+
+
+
++
=
Pfkn
sPFPfk
Pfk
sPFPfk
cADPPfk
sATPPfk
Pfk
Pfk
AK
BPF
L
B
AKPF
K
ADPKATP
PFATPvv
,6,
,6,
,,
,,
max
]6[1
1]6[][
1][
]6][[
(2c)
where
,][][][
1,,,,, bAMPPfkbADPPfkPEPPfk K
AMP
K
ADP
K
PEPA +++=
aAMPPfkaADPPfk K
AMP
K
ADPB
,,,,
][][1 ++=
2.2.4. GAPDH
The rate equation for glyceraldehyde 3-phosphate
dehydrogenase (GAPDH) may be expressed as [7]
+
+
+
+
=
1][
][1
][
1][
][1
][
][][][
,
,
,
,
,
max
NAD
NADH
KNADKGAP
K
PGPK
NAD
NADH
K
PGPGAPv
v
NADHGAPDH
NADGAPDH
PGPGAPDH
GAPGAPDH
eqGAPDH
GAPDH
GAPDH (2d)
whereGAPDHv becomes small as [NADH] increases as
shown in Fig.2b, whereGAPDHv decreases as
[NADH]/[NAD] increases.
Fig.2b Effect of NADH/NAD on GAPDHv
2.2.5. Pyruvate kinaseThe pyruvate kinase (Pyk) reaction is catalyzed by
two isoenzymes such as PykI and PykII each encoded
by pykF and pykA, respectively. PykI is dominant and
activated by FDP and inhibited by ATP, whereas
minor PykII is activated by AMP. Here, we lumped
these together, and the rate equation may be expressed
as [7]
( )ADPPyk
n
PEPPyk
n
AMPPykFDPPyk
ATPPyk
PykPEPPyk
n
PEPPyk
Pyk
Pyk
KADPK
PEP
K
AMP
K
FDP
K
ATP
LK
ADPK
PEPPEPv
v
Pyk
Pyk
Pyk
,
,
,,
,
,
1
,
max
][1][
1][][
][1
][1][
][
+
++
++
+
+
=
(2e)
wherePykv increases as [FDP] increases. Fig.2c shows
the effect of [FDP] on Pykv with respect to [PEP] at theconstant value of [ATP], [ADP] and [AMP], where
Pykv increases little as [FDP] increases in the range of
concern.
Fig.2c Effect of [FDP] on Pykv
2.2.6. PEP carboxylase
It is quite important to correctly simulate the fluxes
at the branch point of PEP, where the enzyme activities
of Pyk and Ppc determine the fluxes. It has been
known that Ppc exhibits a hyperbolic function with
respect to PEP, and that the reaction rate is usually low
without any activator, where AcCoA is a very potent
activator, and FDP alone exhibits no activation, but it
gives strong synergistic activation with AcCoA [10].
Those may be taken into account for the rate equation
[11] as
+++
+++=
][
][
][][1
]][[][][
65
4321
PEPK
PEP
FDPKAcCoAK
FDPAcCoAKFDPKAcCoAKKv
m
Ppc (2f)
Although CO2 is the cosubstrate in Ppc reaction, the
effect of CO2 was not considered in Ppcv . Fig.2e shows
the effect of [AcCoA] onPpcv with respect to [PEP],
where it shows thatPpcv increases as [AcCoA]
increases.
The reverse reaction to Ppc, Pck may be considered
[12, 13], but not shown here.
2.2.7. PDHFor the rate equation of pyruvate dehydrogenase
complex (PDHc) encoded by aceE, F and lpdA, the
hyperbolic function with respect to PYR was
considered, and the inhibition by NADH/NAD was
also taken into account [14]
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++
++
+
+
=
AcCoAmCoAmNADHmNADmPYRm
CoAmNADmPYRmi
PDH
PDH
K
AcCoA
K
CoA
NAD
NADH
KKNADK
PYR
K
CoA
KK
PYR
NAD
NADHK
v
v
,,,,,
,,,
max
][][1
][
][11
][
1][1
][1][
][
][1
1
(2g)
2.2.8. Acetate formation
The acetate formation is of important concern in thecell growth and the specific metabolite production in
E.coli. The main pathway for acetate production is Pta-
Ack pathway, where the reaction catalyzed by Pta and
Ack proceeds through an unstable, high energy acetyl
phosphate (Ace-P). For Pta reaction, the following
equation was considered [14] based on Hankin and
Abales [15]:
++++++
=
CoAiACPmPmAcCoAiCoAiACPiPiAcCoAi
eqpmAcCoAi
Pta
Pta
KK
CAOACP
KK
PAcCoA
K
CoA
K
ACP
K
P
K
AcCoA
K
CoAACPPAcCoA
KKv
v
,,,,,,,,
,,
max
]][[]][[][][][][1
]][[]][[
1
(2h)
The rate equation for Ack reaction was assumed to be
expressed as follows [14]:
++
++
=
ATPmADPmACmACPm
eqACPmADPm
Ack
Ack
K
ATP
K
ADP
K
AC
K
ACP
K
ATPACADPACP
KKv
v
,,,,
,,
max
][][1
][][1
]][[]][[
1
(2i)
2.2.9. ICDH
In E.coli, NADPH is formed in ICDH reaction, and
the activity is inhibited by NADPH. The following
equation was considered [16] in the present study:
1
][
2,
,
][]][2][[]][[
A
ICDHK
COKGNADPHNADPICIK
K
k
v
ICDH
eq
NADPd
ICIm
f
ICDH
=
(2j)
where
2
2
2
22
2
2
2
2
22
2
,
2
,,
,,,,
,,
,,,
,2
,
2
,
,,
,
,,,,
,,
,
2
,,,
,,
,,,
,
,,,,,,
,
1
][][][
][][]][[][][
][][][][][
][][]][[][][1
COdKGmNADPHenhe
NADPeknCOdNADPHenheKGm
COekeNADPHm
COdNADPHenheKGm
NADPHm
COdNADPHenhe
COdNADPHenhe
COm
KGmCOdNADPHenheKGm
COekeNADPHm
COdCOdNADPHenheKGm
COmKGeknh
NADPHemhNADPdICIm
NADPm
ICIdNADPdICImNADPdNADPdICIm
NADPm
K
CO
K
KG
K
NADPH
K
NADPH
KKK
KKKG
KKK
KCOKG
K
CO
K
NADPH
KK
KNADPH
K
KG
KKK
KKKG
K
CO
KKK
KKNADPH
KKK
KNADPH
K
ICI
KK
NADPICI
K
NADP
KK
KICIA
+
+++
++++
++++=
2.2.10. Fermentative pathway
The following equation was used for LDH reaction
[14]:
++
++
=
NADmNADHmLACmPYRm
eqNADHmPYRm
LDH
LDH
KNAD
NADH
KNADK
LAC
K
PYR
K
LAC
NAD
NADHPYR
KKV
v
,,,,
,,
max
1
][
][1
][
1][][1
][
][
][][
1
(2k)
whereLDHv iscreases as NADH/NAD increases. Fig.2d
shows the effect of NADH/NAD onLDHv with respect
to [PYR], whereLDHv increases as NADH/NAD
increases.
Fig.2d Effect of NADH/NAD on LDHv
The equations for ethanol formation from AcCoA
was expressed as [14]
++++
++
=
CoAmAcAldmAcAldmCoAmAcCoAmNADHmNADm
eqNADHmAcCoAm
AALDH
AALDH
KK
CoAAcAld
K
AcAld
K
CoA
K
AcCoA
NAD
NADH
KKNAD
K
AcAldCoA
NAD
NADHAcCoA
KKV
v
,,,,,,,
,,
max
]][[][][][1
][
][11
][
1
]][[
][
][][
1
(2l)
and
++
++
=
ETHmAcAldmNADHmNADm
eqNADHmAcAldm
ADH
ADH
K
ETH
K
AcAld
NAD
NADH
KKNAD
K
ETH
NAD
NADHAcAld
KKV
v
,,,,
,,
max
][][1
][
][11
][
1
][
][
][][
1
(2m)
where those increase as NADH/NAD increases. Fig.2eshows the effect of NADH/NAD on
ADHv with respect
to [AcAld], whereADHv increases as NADH/NAD
increases.
Fig.2e Effect of NADH/NAD on ADHv
2.2.11. PP pathway
For G6PDH and PGDH in the PP pathway, the
following equations [7] were employed:
( )
+
+
++
=
][][
1][
1]6[
]][6[
,,6
,6
6,,6
6,6
max
66
NADPK
NADPHK
K
NADPHKPG
NADPPGVv
NADPHinhNADPHPDHG
NADPPDHG
PinhGNADPHPDHG
PGPDHG
PDHGPDHG
(2n)
and
( )
+
+++
=
ATPinhPGDHNADPHinhPGDH
NADPPGDHPGPGDH
PGDHPGDH
K
ATP
K
NADPHKNADPKPG
NADPPGVv
,,
,6,
max
][1
][1][]6[
]][6[
(2o)
2.2.12. Other rate equationsOther rate equations for Ald, Pgk, CS, 2KGDH,
SDH, Fum, MDH were also considered but not shown
here due to space limitation.
2.3. Effect of oxygen level on the metabolism
It is quite important to grasp the relationship
between oxygen level and the metabolism, since the
oxygen level affects both cell growth and the specific
metabolite production. For example, the following
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strategy is often employed in practice: Initially aerobic
condition was employed to enhance the cell growth,
and then changed to micro-aerobic or anaerobic
condition for the efficient metabolite production. It is,
therefore, desired to simulate the effect of oxygen level
on the metabolism. Escherichia coli possesses the
specific sensing/regulation systems for the rapidresponse to the availability of oxygen and the presence
of other electron acceptors [17-22]. The adaptive
responses are coordinated by a group of global
regulators, which includes two-component ArcA
(anoxic redox control) system and one-component Fnr
(fumarate, nitrate reduction). It has been known that
although the concentration of Fnr protein is similar in
both aerobic and anaerobic conditions [18, 23], it
becomes active only in the anaerobic growth condition.
On the other hand, ArcA/B system works at micro-
aerobic condition. The cytoplasmic ArcA regulator
with its cognate sensor kinase ArcB regulates such
genes that encode several dehydrogenases of theflavoprotein, terminal oxidases, TCA cycle enzymes,
glyoxylate enzymes etc. in response to deprivation of
oxygen [24-26].
Under micro-aerobic or anaerobic condition, PYR is
the important branch point, where LDH, PDHc, and Pfl
compete for it. As the oxygen level decreases, the
redox ratio NADH/NAD increases, and it affects the
flux through LDH and PDH by enzyme level
regulation. Since PDHc is repressed whereas Pfl is
activated by both ArcA and Fnr as the oxygen level
decreases, the effect of oxygen level on these fluxes
may be expresses by the relationship as given in Fig.3a,
where it indicates gene level regulation [27].
0 10 20 30 40
0
2
4
6
8
10
12
[m
m
olg-
1h-
1]
% of aerobiosis
PFL flux
PD H flux
Fig.3a Effect of oxygen level on PDH and Pfl fluxes
(symbols are the experimental data)
The effect of oxygen level on arcA and fnr gene
expressions may be obtained as given in Fig.3b [28].
The effects of ArcA and Fnr on the metabolic pathway
genes such asgltA, acnA,B, icdA, sucABCD, sdhCDAB,
fumA,C, mdh, cyo, cydetc. may be obtained (data not
shown). Those relationships were reflected to modulate
maxv in the reaction rate equations.
0 2 4 6 8 10
100
150
200
250
300
350
0
50
100
150
200
250
300
arcA
expression
relative
to
10
%
O
2
% of aerobiosis
fnrexpression
relative
to
10
%
O
2
Fig.3b Effect of oxygen level on arcA and fnrgene
ecpressions
In order to simulate the effect of oxygen level on
the TCA cycle activation, it is critical to model the
respiratory chain reactions. It may be able to calculate
the distributions of the respiratory flux for the
cytochrome bd and bo terminal oxidases. The kinetic
parameters for Cyd is as follows: Km=0.024 MO2,
vm=42 mol of O2.nmol of Cyd-1.h-1, while those of
Cyo is as follows: Km=0.2 MO2, vm=66 mol of
O2.nmol of Cyo-1.h-1 [29]. Then the flux of electrons to
oxygen (qO2) may be estimated as given in Fig.4 [24],
where qO2 decreases as the oxygen level decreases, and
the amount of NADH utilized for ATP production
reduces. Thus NADH/NAD ratio tends to increase as
the oxygen level decreases, which in turn forces the
fermentative pathways to be activated.
0 20 40 60 80 100
0
1
2
3
4
5
6
qO
2
[m
m
olg-
1h-
1]
% of aerobiosis
Fig.4 Effect of oxygen level on qO2
3. Result
Figure 5 shows part of the simulation result for the
batch culture ofE.coli, where the parameter values
used for the simulation is listed in Table 1. The kinetic
parameter values were employed from the literature as
given in Table 1 exceptmax
v , where denotes the
enzyme name.
max
v was estimated from the flux dataand the measured intracellular metabolite concentration
in the chemostat culture [7,30-33].
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Table 1 Model Parameters
Enzyme Kinetic parameter valuesOriginalsource
Cell
growth1
max 25.0
= h , mMKs 0.1=
PTShgDCWmolmv
PTS./739.25max = mMK aPTS 11, =
mMK aPTS 01.02, = 13, =aPTSK
46, =PGPTSn
mMK PGPTS 5.06, =
[7]
G6PDH
hgDCWmolmv PDHG ./979.0max
6 =
mMK PGPDHG 07.06,6 =
mMK NADPPDHG 015.0,6 =
mMK NADPHinhNADPHPDHG 01.0,,6 =
mMK PinhGNADPHPDHG 18.06,,6 =
[7]
PGDHhgDCWmolmvPGDH ./81.1
max=
mMK PGPGDH 1.06, = mMK NADPPGDH 028.0, = mMK NADPHinhPGDH 01.0, =
mMK ATPinhPGDH 3, = [7]
PfkhgDCWmolmv
Pfk./936.26max =
mMK sPFPfk 14.0,6, = mMK sATPPfk 16.0,, =
mMK aADPPfk 239,, = mMK bADPPfk 25.0,, =
mMK cADPPfk 36.0,, =
mMK aAMPPfk 74.8,, =
mMKbAMPPfk
01.0,, =
mMKPEPPfk
25.0, =
4000000=Pfk
L 4=Pfkn
[7]
AldhgDCWmolmvAld ./461.64
max=
mMK FDPAld 133.0, = mMK DHAPAld 088.0, =
mMK GAPAld 088.0, = mMK GAPinhAld 6.0, =
2, =blfAldV mMK eqAld 1.0, =
[7]
GAPDH
hgDCWmolmvGAPDH ./582.10max
=
mMK GAPGAPDH 15.0, = mMK PGPGAPDH 1.0, =
mMK NADGAPDH 45.0, = mMK NADHGAPDH 02.0, =
63.0, =eqGAPDHK
[7]
Pgk
hgDCWmolmvPgk ./84.158max
= 1800, =eqPgkK
mMK PGPPgk 006.0, = mMK PGPgk 17.03, =
mMK ADPPgk 18.0, = mMK ATPPgk 24.0, =
[7]
EnohgDCWmolmvEno ./439.12
max=
4, =eqEnoK
mMK PGEno 1.02, = mMK PEPEno 135.0, =
[7]
Pyk
hgDCWmolmvPyk ./085.1max
= 1000=PykL
mMK PEPPyk 31.0, = mMK ADPPyk 26.0, =
mMK ATPPyk 5.22, = mMK FDPPyk 19.0, =
mMKAMPPyk
2.0, =
4=Pykn
[7]
PDHhgDCWmolmvPDH ./
max= mMK PYRm 1, =
mMK NADm 4.0, = mMK CoAm 014.0, =
mMK AcCoAm 008.0, = mMK
NADHm1.0, =
mMKi 4.46=
[14]
LDH
hgDCWmolmvLDH ./762.7max
= 7.21120=eqK
mMK NADHm 08.0, = mMK PYRm 5.1, = mMK NADm 4.2, =
mMK LACm 100, =
[14]
Pta
hgDCWmolmvPta ./665.45max
= 0281.0=eqK
mMK AcCoAi 2.0, =
mMK Pm 6.2, =
mMK Pi 6.2, =
mMK AcPm 7.0, = mMK AcPi 2.0, =
mMK CoAi 029.0, = mMK CoAm 12.0, =
[14]
AckhgDCWmolmvAck ./36.875
max=
mMK AcPm 16.0, = mMK ADPm 5.0, =
[14]
mMK ACm 7, = mMK ATPm 07.0, =
2.174=eqK
ALDH
hgDCWmolmvALDH ./69001.0max
=
mMK AcCoAm 007.0, = mMK NADHm 025.0, =
mMK NADm 08.0, = mMK CoAm 008.0, =
mMK AcAldm 10, = 1=eqK
[14]
ADHhgDCWmolmvADH ./928.12
max=
mMK AcAldm 03.0, = mMK NADHm 05.0, =
mMK NADm 08.0, = mMK ETHm 1, = 9.12354=eqK
[14]
CShgDCWmolmvCS ./0675.1
max=
mMK AcCoACS 01.0, = mMK OAACS 007.0, =
mMK CoAi 11.0, =
[33]
ICDH
mMKeq 1000=1min4830 =fk
mMKiCiT
m0059.0= mMK
NADP
d0013.0=
mMKNADPm
0227.0= mMKNADPH
d12.0=
mMKiCITd 03.0= mMK
KG
m038.02 =
mMKiCiTm
0059.0= mMKKG
eknh5.52 =
mMKCO
d6.12 = mMK
CO
eke6.12 =
mMKNADPekn
00016.0= mMKNADPH
m0036.0=
mMKNADPH
enhe 028.0=
[16]
2KGDH
hgDCWmolmv KGDH ./3677.2max
2 = 5.1=KZ
mMK KGKGDH 00.12,2 = mMK CoAKGDH 002.0,2 =
mMK NADKGDH 07.0,2 = mMK KGi 75.02, =
mMK SUCi 0.1, = mMK NADHi 018.0, =
[33]
SDHhgDCWmolmVSDH ./5622.1
max
1 =
hgDCWmolmVSDH ./max
2 =
mMK SUCSDH 10.0, = 0.10, =eqSDHK
[33]
FumhgDCWmolmVFum ./98636.0
max
1 =
hgDCWmolmVFum ./max
2 =
mMK FUMFum 10.0, = 0.10, =eqFumK
[33]
MDH
hgDCWmolmVMDH ./444.62max
1 =
hgDCWmolmVMDH ./max
2 =
mMK NADMDH 10.0, = mMK MALMDH 33.1, = mMK NADHMDH 04.0, =
mMK OAAMDH 27.0, =
mMK NADi 31.0, = mMK MALi 30.3, =
mMK NADHi 04.0, = mMK OAAi 27.0, =
31.0, =lAiK 17.0, =lQiK
0.1, =eqMDHK
[33]
Ppc
hgDCWmolmvPpc ./max
=mMK
PEP
m3231.0=
03176.01 =k mMk 2878.12 =
mMk 05425.03= mMk 8139.0
4=
mMk 0939.05= mMk 2693.0
6=
[11]
Fig.5 shows that cells grow exponentially in
response to the glucose consumption, and how the
intracellular metabolite concentrations change. Fig.5indicates that [PEP] is low throughout batch culture
due to its utilization in PTS. Moreover, all the
intracellular metabolite concentrations were on the
order of 0.1~2.5, which are quite reasonable from the
view point of experimental data. Although the
changing alters of intracellular metabolite
concentration in the glycolysis are reasonable, those in
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the TCA cycle may be somewhat different from the
real behavior. This has to be refined in the near future.
Fig.5 Simulation result for the batch culture
4. Discussion
Although semi-quantitative models were considered
using some experimental data, the developed model
could simulate how the decrease in oxygen level
affects the fermentation patterns in view of
NADH/NAD ratio. Moreover, the overall ATP
produced can be also computed and this can be used to
estimate the cell growth rate by taking into account the
biosynthetic equation as well. The present modeling
approach is new and can be used in practice for
performance improvement and the design of cell
metabolism.
5. Conclusion
It was shown that the kinetic models considered in
the present research can be used for the simulation of
the batch culture of both aerobic and anaerobic
conditions.
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