art%3a10.1007%2fbf00173913
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Ap pl M icrobiol Biotech nol (1994) 42:508-515 Springer-Ve rlag 1994
O R I G I N A L P A P E R
J . A . d e H o l l a n d e r
otent ia l m etabol ic l im i tat ions in lys ine prod uct ion by o r y nebac t e r i um
g l u t am i c um s rev eale d by m etabol ic network analys is
Rece ived: 11 Ap ril 1994 / Ac cepted: 10 May 1994
bstract
A n a l y s i s o f t h e m e t a b o l i c n e t w o r k o f ly s in e -
p r o d u c i n g
Corynebacterium glutamicum
s h o w e d t h a t
l y s i n e y i e l d s a r e l i m i t e d b y t h e e x c e s s e n e rg y p ro d u c -
t i o n i n l y s i n e b i o s y n t h e s i s . Th e m o s t p ro b a b l e m a x i -
m u m y i e l d is 0. 47 m o l / m o l o n g l u c os e , w h e n p h o s p h o e -
nolpyruvate
c a rb o x y l a s e fu n c t i o n s i n a n a n a p l e ro t i c
r e a c t i o n . W h e n t h is f u n c t i o n i s fu l f i ll e d b y t h e g l y o x y -
l a t e p a t h w a y , a m a x i m u m y i e l d o f 0 . 38 m o l / m o l i s o b -
t a i n e d .
ntroduction
Corynebacterium glutamicum
a n d c l o s e l y r e l a t e d
Brevi
bacterium
s p e c i e s a r e t h e m o s t i m p o r t a n t o r g a n i s m s
u s e d fo r th e i n d u s t r i a l f e rm e n t a t i v e p ro d u c t i o n o f l y -
s i n e . A l t h o u g h w i l d - t y p e s t r a i n s d o n o t e x c re t e l y s i n e a t
a l l , c l a s s i c a l m u t a t i o n p ro g ra m s h a v e r e s u l t e d i n s t r a i n s
p ro d u c i n g a h ig h t i t e r , m a i n l y a s t h e r e s u l t o f a r e l ie f o f
f e e d - b a c k i n h i b it i o n o f t h e k e y e n z y m e a s p a r t a t e k i -
n a s e . Th e y i e l d s o n g l u c o s e a s t h e c a rb o n s o u rc e a r e
v e ry s u b s t a n t i a l: v a l u e s o f 4 0 % ( t o o l / to o l ) o r e v e n h i g h -
e r c a n b e fo u n d i n t h e l i t e r a t u r e (To s a k a e t a l . 1 9 8 3 ;
N a k a y a m a 1 9 8 5 ) . G e n e t i c e n g i n e e r i n g t e c h n i q u e s c a n
b e u s e d t o e n h a n c e t h e a c t i v i t y o f p o t e n t i a l l y r a t e - li m i t -
i n g e n z y m e s . S u c h a n a p p r o a c h w a s s h o w n t o b e s u c -
c e s s fu l w h e n a p p l i e d o n l o w -y i e l d s t r ai n s (C re m e r e t a l.
1 99 1 ). H o w e v e r , i n d ic a t i o n s fo r t h e a p p l i c a t i o n o f t h e s e
t e c h n i q u e s t o t h e p ro d u c t i o n o f h ig h e r -y i e l d i n g i n d u s -
t r i a l s t ra ins a re ha rd to f ind in the case o f ly s ine fe r -
m e n t a t i o n . T h e v e r y h ig h c o n v e r s i o n y i e l d o f t h o s e
s t r a in s i m p l i e s a s u b s t a n t i a l i m p a c t o f l y s in e p ro d u c t i o n
o n t h e m e t a b o l i c p a t t e r n o f t h e p r o d u c i n g c e ll , n o t o n l y
o n t h e l y s i n e -b i o s y n t h e s i s p a t h w a y i t s e l f , b u t a l s o o n
t h e p a t h w a y s o f t h e a u x i l i a ry m e t a b o l i s m . Th i s c o u l d
v e ry w e l l b e a r e a s o n fo r t h e l i m i t e d s u c c e s s o f d i r e c t e d
i m p r o v e m e n t o f p a t h w a y e n z y m e s : t h e r e a l b o t t l e n e c k
J. A. de H ollander
Gist-brocades, PO Box i, 2600 MA Delft, The N etherlands.
FAX: +31-15-792490
m i g h t r e s i d e e l s e w h e r e i n t h e m e t a b o l i s m . M e t a b o l i c
n e t w o rk a n a l y s i s p ro v i d e s a t o o l f o r t h e i n v e s t i g a t i o n o f
p o t e n t i a l m e t a b o l i c b o t t l e n e c k s i n c l u di n g t h o s e o u t s i d e
t h e b i o s y n t h e si s p a t h w a y o f t h e p r o d u c t ( S t e p h a n o p o u -
l o s a n d S i n s k e y 1 9 93 ). I n a d d i t i o n , n e t w o rk a n a l y s is c a n
b e e m p l o y e d t o d e c r e a s e t h e d e g r e e o f f r e e d o m o f a
f e r m e n t a t i o n s y s t e m a n d t o d e r i v e p r e d ic t i v e fe r m e n t a -
t i o n m o d e l s ( d e H o l l a n d e r 1 9 9 1 a , b ) . N e t w o r k a n a l y s i s
w a s u s e d b y V a l l i n o a n d S t e p h a n o p o u l o s (1 9 93 ) to l o -
c a t e c r i t i c a l b r a n c h p o i n t s ( r i g i d n o d e s ) i n t h e m e t a -
b o l i s m o f l y s i n e -p ro d u c i n g C. glutamicum. In th i s a r t i -
c l e b o t t l e n e c k s i n t h e Corynebacterium m e t a b o l i s m a r e
i d e n t i f ie d , r e s u l t i n g f ro m t h e i m p o s s i b i l it y o f n e g a t i v e
f l u x e s t h ro u g h s o m e i r r e v e r s i b l e p a t h w a y s .
Metabol ic network analysis
T h e m e t a b o l i s m o f l y s in e - p r o d u ci n g C o r y n e b a c t e r i u m
Th e m a j o r c h a ra c t e r i st i c s o f l y s i n e - r e l a t e d m e t a b o l i s m
in
C. glutarnicum
a n d r e l a t e d o rg a n i s m s s u c h a s
Brevi
bacterium
s p e c i e s a r e f a i r l y w e l l k n o w n (K i n o s h i t a
1 98 5 ; N a k a y a m a 1 9 8 5) . N e v e r t h e l e s s , a n u m b e r o f i m -
p o r t a n t a s p e c t s r e m a i n u n c e r t a i n . T h e m o s t i m p o r t a n t
u n c e r t a i n t i e s a r e r e l a t e d t o m e t a b o l i s m a u x i l i a ry t o t h e
l y si n e p a t h w a y , s u c h a s t h e g e n e r a t i o n o f N A D P H , t h e
b i o e n e r g e t i c s o f t h e b a c t e r i u m a n d t h e t y p e o f a n a p le -
ro t i c r e a c t i o n t h a t i s u s e d . Th e fo l l o w i n g s h o r t o v e rv i e w
o f l y s i n e m e t a b o l i s m w i l l s t r e s s t h e s e a s p e c t s . F i g u re 1
p re s e n t s a s i m p l i fi e d , s c h e m a t i c o v e rv i e w o f t h e c e l l u l a r
m e t a b o l i s m o f Corynebacterium w i t h e m p h a s i s o n t h e
m a j o r m e t a b o l i c b r a n c h p o i n t s . T h e f i g u r e f o r m s t h e
b a s i s o f t h e m e t a b o l i c f l u x a n a l y s is i n t h e n e x t p a r a -
g ra p h .
F ro m c o n t i n u o u s -c u l t u r e s t u d i e s (S h v i n k a e t a l .
1980 ; Micha l sk i e t a l . 1984 ; Hi rao e t a l . 1989 ; Kiss and
S t e p h a n o p o u l o s 1 9 9 2 ; O h a n d S e rn e t z 1 9 9 3 ) i t c a n b e
c o n c l u d e d t h a t l y s i n e p ro d u c t i o n i s c l o s e l y a s s o c i a t e d
w i t h b a c t e r i a l g ro w t h , i . e . th e s p e c i fi c l y s in e p ro d u c t i o n
ra t e t e n d s t o b e d i m i n i s h e d a t v e ry lo w g ro w t h r a t e s. A
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509
G L U O S E
T P
B I O M A S S ~ J ~ p
M [ H M P
j - co2
N M H ~
ATP V
P E P
~ - ~ T P
C 2
C 2
~
I C I T
= A o g '. . . . . 1 ) - -
S y s/ S ~ C A
ATP-~
L Y S I N E e
Fig. 1 Metabo l ic pa thway s in lys ine -produc ing Cory nebac te r ium
glu tamicum. EM E m b d e n -Me y e rh o f , HMP h e x o s e m o n o p h o s -
pha te ,
G6P
glucose 6 -phospha te ,
PEP phosphoenolpyruvate,
PYR
pyruva te ,
OAA
oxa loace ta te ,
ICIT
isocitrate ,
SUC
succi-
hate ,
SUCA
s u c c in y l -C o A
d i s c u s s i o n o f t h e o r e t i c a l l y p o s s i b l e l y s i n e y i e l d s i s
t h e r e f o r e r a t h e r u s e l e s s w h e n l y s i n e p r o d u c t i o n i s n o t
c o n s i d e r e d w i t h i n t h e c o n t e x t o f t h e o v e r a l l b a c t e r i a l
m e t a b o l i s m . T h i s a d d s q u i t e a f e w u n c e r t a i n t i e s t o t h e
q u e s t i o n o f t h e o v e r a l l s t o i c h i o m e t r y o f l y s i n e p r o d u c -
t i o n .
A r e c e n t s t u d y ( S o n n t a g e t al . 1 9 9 3) c o n f i r m e d t h a t
t w o v a r i a n t s o f t h e l y s in e - p r o d u c in g d i a m i n o p i m e l a t e
p a t h w a y e x i s t i n
Corynebacterium
w h i c h m a y b e a c t i v e
s i m u l t a n e o u s l y , d e p e n d i n g o n t h e c o n d i t i o n s . E n e r g e t i -
c a l l y t h e r e i s a s m a l l d i f f e r e n c e b e t w e e n t h e p a t h w a y s ,
w h i c h i s p a r t l y d e p e n d e n t o n t h e m e a n s o f a m m o n i a
a s s i m i l a t i o n , f o r w h i c h t w o p a t h w a y s c a n b e p r e s e n t i n
Corynebacterium ( N e i s h t a d t - A b r a m o v i c h e t a l . 1 9 9 0 ,
E r t a n 1 9 9 2) . B y a n a l o g y w i t h o t h e r o r g a n i s m s i t c a n b e
a s s u m e d t h a t t h e e n e r g y - r e q u i r i n g g l u t a m a t e s y n t h a s e
r e a c t i o n i s p r e f e r r e d a t l o w o r l i m i t i n g a m m o n i a c o n -
c e n t r a t i o n s , w h i l e a t h i g h e r a m m o n i a c o n c e n t r a t i o n s
t h e g l u t a m a t e d e h y d r o g e n a s e r e a c t i o n i s a c t i v e . F o r
c o n d i t i o n s o f l y si n e p r o d u c t i o n i t i s n o t u n r e a s o n a b l e t o
a s s u m e t h a t t h e l a t t e r r e a c t i o n p r e d o m i n a t e s .
A p o i n t o f c o n t r o v e r s y i s t h e q u e s t i o n o f w h i c h ( a n a -
p l e r o t i c ) r e a c t i o n i s r e s p o n s i b l e f o r t h e f o r m a t i o n o f o x -
a l o a c e t a t e . T h e g l y o x y l a t e p a t h w a y i s s o m e t i m e s p r o -
p o s e d t o f u l f il l t h i s r o l e i n l y s i n e b i o s y n t h e s i s ( S h v i n k a
e t a l. 1 9 8 0 ); h o w e v e r , w h e n g l u c o s e is th e m a i n c a r b o n
s o u r c e t h e a c t i v i t y o f t h e c r i t i c a l e n z y m e i s o c i t r a t e l y a s e
i s o f t e n l o w ( V a l l i n o a n d S t e p h a n o p o u l o s 1 9 9 3 ) a n d i n
s o m e s p e c i e s t h e e n z y m e i s i n d u c e d o n l y i n t h e p r e s -
e n c e o f a c e t a t e ( R u k l i s h a e t a l. 1 9 78 ) . T h e m o s t p r o b a -
b l e a l t e r n a t i v e i s t h e phosphoenolpyruvate ( P - p y r u -
v a t e ) c a r b o x y l a s e r e a c t i o n , w h i c h i s f o u n d t o b e p r e s e n t
i n h i g h a c t i v i t y i n Corynebacterium. P - p y r u v a t e c a r -
b o x y l a s e h a s b e e n t h e t a r g e t i n a d i r e c t e d s t r a i n - i m -
p r o v e m e n t s t u d y ( S a n o e t a l . 1 9 8 7 ) . I t s r o l e i s n o t u n e -
q u i v o ca l ly p r o v e n , h o w e v e r , b e c a u s e d e l e t io n m u t a n t s
m i s s i n g a n y a c t i v i t y s t i l l p r o d u c e d l y s i n e a t t h e s a m e
y i e l d ( P e t e r s - W e n d i s c h e t a l. 1 99 3 ). A n u m b e r o f o t h e r
a l t e rn a t i v e s c a n b e t h o u g h t o f , s u c h a s t h e r e a c t i o n s c a -
t a l y z e d b y p y r u v a t e c a r b o x y l a s e , P - p y r u v a t e c a r b o x y -
k i n a s e , o r m a l i c e n z y m e . I n t h e i r o v e r a l l s t o i c h i o m e t r y
t h e y a r e s i m i l a r t o t h e P - p y r u v a t e c a r b o x y l a s e r e a c t io n ,
a n d n o n e o f t h e m w i l l b e i n c l u d e d i n t h e p r e s e n t d i s cu s -
s ion .
N A D P H i s u s e d i n s e v e r a l r e a c t i o n s o f l y s i n e b i o -
s y n t h e s i s . T h e c e l l h a s o n l y a l i m i t e d n u m b e r o f p o s s i -
b i l i t i e s t o g e n e r a t e r e d u c t i o n e q u i v a l e n t s i n t h e f o r m o f
N A D P H . A n o b v i o u s p o s s ib i li ty is t h e h e x o s e m o n o -
p h o s p h a t e ( H M P ) p a t h w a y , s h o w n i n F ig . 1 a s a b r a n c h
o f a s p l i t p a t h w a y f o r g l u c o s e c a t a b o l i s m , t h e a l t e r n a -
t iv e f o r t h e E m b d e n - M e y e r h o f p a t h w a y . O n l y
1/6
o f t h e
r e d u c t i o n p o t e n t i a l o f g l u c o s e i s t r a n s f o r m e d i n t o
N A D P H v i a t h is r o u te , h o w e v e r . M o r e e f f ic i en t w o u l d
b e t h e o p e r a t i o n o f th e c y c li c f o r m o f t h e H M P p a t h -
w a y , w h i c h g i v es 1 0 0 y i e ld o f r e d u c t i o n e q u i v a l e n t s i n
t h e f o r m o f N A D P H . F o r c y cl ic o p e r a t i o n o f t h e H M P
p a t h w a y t h e g l u c o n e o g e n i c e n z y m e f r u c t o se - l, 6 -b i s -
p h o s p h a t a s e i s r e q u i r e d . A c t i v i t y o f t h i s e n z y m e i s i n -
c o m p a t i b l e w i t h t h e s i m u l t a n e o u s o p e r a t i o n o f t h e
E m b d e n - M e y e r h o f p a t h w a y , a n d i s n o r m a l l y r e p r e s s e d
u n d e r c o n d i t io n s o f g r o w t h o n g l u co s e . A n o t h e r p o s si -
b l e m e t h o d o f N A D P H g e n e r a t i o n is t h e r e a c ti o n c a ta -
l y z e d b y t h e e n z y m e i s o c i t r a t e d e h y d r o g e n a s e , w h i c h i s
u s u a l l y c o n s i d e r e d t o b e N A D P - d e p e n d e n t i n Coryne-
bacterium.
T h e t w o m o s t i m p o r t a n t c e l lu l a r t r a n s p o r t p r o c e s s e s
i n l y s i n e f o r m a t i o n , g l u c o s e u p t a k e a n d l y s i n e e x c r e -
t i o n , a r e b o t h e n e r g y - d r i v e n . F o r g l u c o s e u p t a k e t h e
p h o s p h o t r a n s f e r a s e s y s t e m i s e m p l o y e d ( M o r i a n d
S h i i o 1 9 8 7 ; M a l i n a n d B o u r d 1 9 8 7 ) , w h i c h u t i l i z e s t h e
h i g h - e n e rg y p h o s p h a t e g r o u p f r o m P - p y r u v a t e . A l -
t h o u g h m e t a b o l i c e n e r g y i s u s e d f o r g l u c o s e t r a n s p o r t ,
t h e r e a c t i o n i s e n e r g y - e f f ic i e n t b e c a u s e g l u c o s e i s d e li v -
e r e d i n p h o s p h o r y l a t e d f o r m . T h e r e a c t i o n i s t h e r e f o r e
e n e r g e t i c a l l y e q u i v a l e n t t o p h o s p h o r y l a t i o n o f g l u c o s e
t o g l u c o s e 6 - p h o s p h a t e b y A T P , a s s h o w n i n F ig . 1 . I n
h i g h - p r o d u c i n g s t r a in s o f Corynebacterium l y s ine i s ex -
c r e te d th r o u g h a O H - s y m p o r t s y s te m ( B ro ~ r an d
K r i m e r 1 99 1; K r i m e r 1 9 9 4 ), w h i c h i m p l i e s t h a t , a ss o -
c i a t e d w i t h l y s i n e e x c r e t i o n , m e t a b o l i c e n e r g y ( A T P
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a b l e 1 Reactions of the metabolism of Corynebac ter ium g lu -
t a m i c u m as displayed in Fig. 1. Reactions are formulated in a sim-
plified manner, excluding the oxidized counterparts of the reduc-
tance carriers (NAD, NADP and FAD), and the de-energized
counterpart of ATP (ADP). A number of (alternative) reactions
are commented on in the text E M Embden-Meyerhof, H M P
hexose monophosphate, T C A tricarboxylic acid, Oaa oxaloace-
tate, P r y pyruvate, Suc succinate, Glc glucose. P P r v p h o s p h o e n o l -
pyruvate, iC i t isocitrate)
Lysine biosyntheis
Lysine excretion
Glucose uptake
EM pathway
Cyclic HMP pathway
HMP pathway
Pyruvate kinase
TCA pathway
n a p l e r o t i c r e a c t io n
O x i d a t iv e p h o s p h o r y l a t i o n
B i o m a s s f o r m a t i o n
Oaa + Pry + 2NH3 + Suc-CoA + ATP + 4 NADPH ~ Lys + Suc + CO2
Oaa + Pry + 2 NH3 + Suc-CoA + 3 ATP + 4NADPH --, Lys + Suc + CO2
Oaa + Pry + 2NH3 + ATP + 4NADPH --, Lys + CO2
Oaa + Pry + 2NH3 + 2 ATP + 4 NADPH ~ Lys + CO2
Lys + al ATP ~ Lysc
Glc + ATP --, Glc6P
Glc6P ~ 2 PPrv + ATP + 2 NADH
Glc6P --, 6 COz + 12 NADPH
Glc6P --, % PPrv + CO2 + ATP + 2NA DPH + % NADH
PPrv -~ Prv+ ATP
Prv + Oaa --* iCit + CO2 + NADH
iCit --, Suc-CoA + 2 CO2 + 2 NADH
iCit --, Suc-CoA + 2 CO2 + NADH + NADPH
Suc-CoA ~ Suc + ATP
Suc --, Oaa + NADH + FADH
PPrv + CO2 ---, Oaa
2 Prv ~ Oaa + 2 CO2 + 4N ADH + FADH
NADH + 02 ~ P/O ATP + H20
FADH + 02 --' 9/3 P/O ATP + H20
o-Glc + cnxNH3 + 6ax ATP ~ 6X + 6(o--1)CO2 + (12 o-- 3yx )NADH
l a a
lb
lc
ld
2
3
4a
4b
5
6
7
8a
8b
9
10
11a
11b
12
13
14
a Reaction equations wi th the same number but with different letters represent metabolic alternatives, of which only one can be
active
equivalents) is used for the restoration of the mem-
brane potential.
Although some energy is used in the biosynthesis of
lysine and its excretion, the overall balance within the
context of the cellular metabolism is positive if one in-
cludes the AT P generated during oxidation of NADH ,
which is produced in the reactions leading to formation
of the precursors of the lysine pathway. This energy-
generating property of lysine biosynthesis might pro-
vide an explanation for the apparent association of ly-
sine for mation with cell growth, because biosynthesis of
new cell material is the normal process in which ATP is
utilized. The efficiency of energy genera tion (oxidative
phosphorylation) and efficiency of growth are therefore
an important factors that determine, to a large extent,
the maximum possible conversion yields, as will be il-
lustrated later.
A stoichiometric model for bacterial growth and
lysine production
The lysine fermentation system is considered, in simpli-
fied form, to be a reaction producing biomass and ly-
sine from glucose and ammonia. Elemental mass bal-
ance considerations pr ovide restrictions for the flows of
reactants. The de gree o f free dom of the system is deter-
mined by the numbe r of reactants minus the number of
mass balance equations (Roels 1983). The reactions
constituting the cellular metabolism form a network.
Network relationships provide further restrictions for
the metabolism, which reduce the degree of freedom of
the system. In a previous publication (de Hollander
1991a) it was concluded that the best way to explore
these restrictions is by expressing the network as a ma-
trix equation and by employing basic linear algebra
methods, as has also been done by a number of other
authors. Following the methodology described earlier,
the macroscopic flows of the system are divided into
primary flows and secondar y flows, the latter following
from the former through elemental mass balance rela-
tionships. For the lysine fermentation system the flows
of glucose, biomass and lysine are defined as primary
flows; flows of oxygen, carbon dioxide and ammonia
follow from the carbon, nitrogen and degree of reduc-
tance balance. Metabolic net work restrictions, based on
a pseudo-steady-state assumption for all intermediates,
can be used to derive a balance equation for the prima-
ry external flows. The network expression is obtained
by filling the rows of a matrix Z with the stoichiometric
coefficients of the reactions displayed in Fig. 1. In prin-
ciple only equations for reactions between metabolic
branch points are included. In most cases these equa-
tions are lumped equations, involving a few or many
individual enzymatic steps. For a number of reactions
alternative expressions are formulated, because of the
uncertainties discussed earlier. Stoichiometric coeffi-
cients related to the cellular energy metabolism are not
known exactly; these coefficients (as well as a few oth-
ers) are included as parameters.
The reaction equations are summarized in Table 1.
A num ber of reactions represent alternatives for the
metabolism; they have been given the same number
with a letter for discrimination.
For lysine biosynthesis four possible equations are
consider ed. The reacti on in Eq. la in Table 1 is the
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o v e ra l l e q u a t i o n fo r t h e s u c c i n y l a s e v a r i a n t o f t h e d i a m -
i n o p i m e l a t e p a t h wa y , i n c l u d i n g t h e a m m o n i a a s s i m i l a -
t i o n r e a c t i o n . F o r t h e d e h y d ro g e n a s e v a r i a n t s , s u c c i n y l -
C o A a n d s u c c i n a t e m u s t b e o m i t t e d ( E q . l c , d ) . W h e n
a m m o n i a a s s im i l a ti o n o c c u r s v i a t h e e n e r g y - r e q u i r i n g
g l u t a m i n e s y n t h a s e r e a c ti o n , t h r e e o r t w o A T P i n s t e a d
o f o n e m u s t b e i n c l u d e d f o r t h e s u c c in y l a se a n d t h e d e -
h y d ro g e n a s e v a r i a n t s r e s p e c t i v e l y (E q . 1 , d ) . Ac c o rd i n g
t o t h e m e c h a n i s m p r o p o s e d b y B r o ~ r a n d K r ~im e r
( 1 9 9 4 ) t w o p r o t o n s m u s t b e t r a n s l o c a t e d f o r e v e r y l y -
s i n e m o l e c u l e t h a t i s e x c re t e d . A s t h e e f f i c i e n c y o f e le c -
t r o n - t r a n s p o r t- d r i v e n p r o t o n t r a n s l o c a ti o n i s n o t
k n o w n , a p a r a m e t e r a~ i s i n c l u d e d i n e q . 2 t o r e p re s e n t
t h e e n e r g y c o s t s . A s a d e f a u l t v a l u e a ~ = l w a s a d -
o p t e d .
T h e E m b d e n - M e y e r h o f p a t h w a y a n d t h e c y cl ic f o r m
o f t h e H M P p a t h w a y a r e c o n s i d e r e d t o b e m u t u a l l y e x -
c l us iv e . T h e l i n e ar H M P p a t h w a y i s c o n s i d e r e d t o c o v e r
t h e s e q u e n c e f r o m g l u c o s e 6 - p h o s p h a t e t o p h o s p h o e -
nolpyruvate.
B e c a u s e f o u r b r a n c h i n g p o i n t s a r e i d e n ti f -
i e d i n t h e t r i c a rb o x y l i c a c i d p a t h w a y ( s e e F i g . 1 ), t h e
p a t h w a y i s e x p r e s s e d b y f o u r e q u a t i o n s .
A c o m p l e t e b u t b r a n c h e d r e s p i r a t o r y c h a in w i t h
m u l t i p l e o x i d a s e s wa s d e s c r i b e d fo r Brevibacterium fla-
ru m
(S h v i n k a e t a l . 1 97 9) . B e c a u s e o f th i s b r a n c h i n g ,
w i t h s o m e b r a n c h e s b y p a s s i n g p r o t o n t r a n s l o c a t i o n
c e n t e r s , t h e o v e ra l l P / O r a t i o o f t h e o rg a n i s m i s u n c e r -
t a i n , b u t w i l l b e l e s s t h e n t h e m a x i m u m v a l u e fo r a
c o m p l e t e (m i t o c h o n d r i a l - t y p e ) r e s p i r a t o ry c h a i n , as i s
a l so a p p a r e n t f r o m a r e l a ti v e l y l o w H + / O r a t io f o u n d
fo r
Brevibacterium lactofermentum
(Ka wa h a ra e t a l .
1 98 8) . T h e P / O r a t io f o r N A D H o x i d a t io n i s t h e r e f o r e
i n c l u d e d as a p a r a m e t e r . T h e P / O r a t io f o r F A D H o x i-
d a t i o n w a s a s s u m e d t o b e 2/3 o f t h e P / O r a t i o fo r t h e
c o m p l e t e r e s p i r a t o r y c h a in .
B i o m a s s (X) i n e q . 1 4 o f T a b l e 1 i s e x p re s s e d i n C -
m o l u n i t s , t h e a m o u n t c o n t a i n i n g 1 m o l c a rb o n . T h e
n u m b e r o f e n e r g y e q u i v a l e n t s r e q u i r e d f o r t h e s y n th e -
s i s o f 1 m o l C b i o m a s s i s a x , a p a ra m e t e r r e l a t e d t o t h e
m o r e o f t e n u s e d y i e l d o n A T P : ax=Mx/YATp, w h e r e
M x i s t h e we i g h t o f a C -m o l b i o m a s s . T h e c o e f f i c i e n t o -
f o r t h e c a r b o n s o u r c e i n t h i s e q u a t i o n r e s u l t s f r o m t h e
f a c t t h a t c a r b o n d i o x i d e i s p r o d u c e d i n a n u m b e r o f
a n a b o l i c r e a c t i o n s ( n o t t o b e c o n f u s e d w i t h c a t a b o l i c
C O 2 p r o d u c t i o n ) . T h e n u m e r i c a l v a l u e f o r g r o w t h o n
g l u c o s e i s a b o u t 1 . 1 (B a b e l a n d M t i l l e r 1 9 8 5 ; Go m m e rs
e t a l . 1 9 8 8 ) . B i o m a s s fo rm a t i o n f ro m g l u c o s e n o rm a l l y
r e s u l t s i n a s m a l l s u rp l u s o f r e d u c t i o n e q u i v a l e n t s , d e -
p e n d i n g o n o - a n d t h e d e g r e e o f re d u c t i o n o f b io m a s s
(rx).
I n t o t a l , 1 4 m e t a b o l i c r e a c t i o n s h a v e b e e n f o r m u -
l a t e d , i n v o l v i n g 12 k e y i n t e rm e d i a t e s a n d 3 m a c ro s c o p i c
s u b s t a n c e s (g l u c o s e , l y s i n e a n d b i o m a s s ) , e x c l u d i n g t h e
m a c r o s c o p i c s u b s t a n c e s d e f i n e d a s s e c o n d a r y f l o w s .
T h e m e t a b o l i c n e t w o r k e q u a t i o n i s f o r m u l a t e d a s :
Z T R m = R 1 )
wh e re t h e m u l t i p l e o f t h e t r a n s p o s e d (1 4 x 1 5 ) st o i -
c h i o m e t ry m a t r i x Z a n d t h e (1 4 1) v e c t o r R m wi t h m e -
t a b o l i c r e a c t i o n r a t e s fo rm s a (1 5 x 1 ) v e c t o r R w i t h
f l o ws o f e x t e rn a l s u b s t a n c e s a n d i n t e rm e d i a t e s . A s a
c o n s e q u e n c e o f th e p s e u d o s t e a d y s t a te h y p o t h e s i s ( c e l-
l u la r c o n c e n t r a t i o n s o f i n t e rm e d i a t e s a r e a p p r o x i m a t e l y
c o n s t a n t ) , t h e v e c t o r R c o n t a i n s a n u m b e r o f z e ro s ,
w h i c h a l l o w s t h e e v a l u a t i o n o f a m e t a b o l i c b a l a n c e
e q u a t i o n f o r t h e e x t e r n a l f l o w s. T h e m e t h o d u s e d f o r
t h i s b a l a n c e e v a l u a t i o n i s r e l a t e d b u t n o t i d e n t i c a l t o a
p r e v i o u s l y d e s c r i b e d m e t h o d ( d e H o l l a n d e r 1 9 9 1 a ) a n d
m e t h o d s p u b l i s h e d b y o t h e r s ( P a p o u t s a k i s a n d M e y e r
1 9 8 5 ; T s a i a n d L e e 1 9 8 8 ) . T h e l a t t e r a u t h o r s d i d n o t
e v a l u a t e a m e t a b o l i c b a l a n c e e q u a t i o n , h o w e v e r . H e r e
t h e p ro c e d u re i s d e s c r i b e d b r i e f l y i n g e n e ra l t e rm s . L e t
t h e d i m e n s i o n s o f t h e m e t a b o l i c s y s t e m b e a s f o l lo w s : m
re a c t i o n e q u a t i o n s w i t h n b i o c h e m i c a l s p e c i e s ; t h e n u m -
b e r o f c o n s e r v e d s p e c i es ( m e t a b o l i c k e y i n t e r m e d i a t e s )
i s k , wh ich leave s l = n - k n o n - c o n s e r v e d s p e c i e s o r m a -
c ro s c o p i c s u b s t a n c e s . T h e n t h e fo l l o wi n g p a r t i t i o n i n g o f
t h e n e t wo rk e q u a t i o n (E q . 1 ) i s p o s s i b l e :
Zl l Z12
l + n - m ) x l l + n - m ) x m - l )
Z21 Z22
(m - l) l (m - l) (m - l)
R m l
I x 1
Rm2
m - l ) x i
: :
2 )
w h i c h c a n b e w o r k e d o u t t o :
Z R m l = R 1 , w ith Z - - Z l l - Z 1 2 Z ~ l Z 2 1 3 )
C a r e s h o u l d b e t a k e n t h a t, b y a p p r o p r i a t e a r r a n g e-
m e n t o f ro ws a n d c o l u m n s , m a t r i x Z 2 2 i s n o n - s i n g u l a r ,
o t h e rw i s e t h e e v a l u a t i o n o f E q . 3 w i ll fa i l. W h e n n > m
( i. e. t h e m e t a b o l i c s y s t e m i s o v e r -d e t e r m i n e d ) , t h e v e c -
t o r R 1 s t i l l c o n t a i n s a t l e a s t o n e z e ro e l e m e n t , s o t h e
m a t r i x e q u a t i o n c a n a g a i n b e p a r t i t i o n e d :
Z l t m l = t e l 4 )
wh e re Z 1 is a l l s u b m a t r i x r e l a t e d t o e x t e rn a l f l o ws
o n l y , a n d R e 1 i s t h e v e c t o r w i t h p r i m a ry e x t e rn a l f l o ws .
T h e v e c t o r w i t h m e t a b o l i c r e a c t i o n r a t e s t m l c a n b e
e l i m i n a t e d f ro m t h i s e q u a t i o n , r e s u l t i n g i n a b a l a n c e
e q u a t i o n f o r t h e p r i m a r y e x t e r n a l f l ow s :
Z 3 R ~ I = 0 , w i th Z 3 = Z 2 Z ~ - 1 ( 5)
F o r t h e c a s e o f t h e ly s in e f e r m e n t a t i o n ( t h r e e p r i m a -
ry e x t e rn a l f l o ws ) , E q . 5 c a n a l s o b e wr i t t e n a s :
Z i R s b g 2 R x - l -. ~ 3 N p = O ,
o r Rs=l /YxsRx+l /YpsRp
(6)
wh i c h i s t h e f a m i l i a r l i n e a r e q u a t i o n r e l a t i n g t h e c a r -
b o n s o u r c e c o n s u m p t i o n r a t e ( R s) w i th t h e r a t e o f b i o -
m a s s f o r m a t i o n ( R x) a n d t h e r a t e o f p r o d u c t f o r m a t i o n
(Rp) .
T h e y i e ld p a r a m e t e r s f o l l o w f r o m t h e b a l a n c e
e q u a t i o n c o e f f i c i e n t s
as:
Y x s = - g l / g 2 a n d Y p s = - g l / Z 3 .
T h e p a r a m e t e r Yps i s t h e d i f f e r e n t i a l c a rb o n u t i li z a t i o n
e f f i c i e n c y o f l y s in e p ro d u c t i o n ( t h e n e t l y s i n e y i e l d ). I t
s h o u l d b e n o t e d , h o w e v e r , t h a t th i s p a r a m e t e r d o e s n o t
i n d i c a t e t h e m a x i m u m p o s s i b l e c o n v e r s i o n e f f i c i e n c y ,
w h i c h c a n b e r e a c h e d w h e n n o b i o m a s s f o r m a t i o n t a k e s
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Table 2 Differential a nd maximum overall lysine yields for a numb er of variants of C glutamicum metabolism
An aplero tic reaction N AD PH generation Limiting Yps
pathway (mol/mol)
Linear Cyclic ICD H a
H M P H M P
Y ~
(mol/mol)
Phosphoenolpyruvate carboxylase
Glyoxylate pathway
+ - - EM 0.778 0.333
+ - + EM 0.777 0.468
+ + - TC A 0.774 0.727
+ - - EM 0.712 0.353
+ - + EM 0.706 0.382
+ + - TC A 0.709 0.412
a Isocitrate dehyd rogenase
p l a c e . I t w a s a r g u e d t h a t t h e m e t a b o l i c r e a c t i o n s i n -
v o l v e d i n l y si n e p r o d u c t i o n a r e i n t e r l i n k e d w i t h t h e
g e n e r a l m e t a b o l i s m a n d l y s in e p r o d u c t i o n c a n n o t t o t a l -
l y b e u n c o u p l e d f r o m b i o m a s s f o r m a t i o n , u n l e s s a n -
o t h e r w a y o f h y d r o l y z i n g o f A T P is in t r o d u c e d . C a l c u -
l a t e d v a l u e s f o r Y p s a r e i n c l u d e d i n T a b l e 2 .
C a l c u l a t i o n o f in t e r m e d i a r y r e a c t i o n r a t e s a n d
m a x i m u m l y s in e y ie l d s
T h e m e t a b o l i c n e t w o r k e q u a t i o n ( E q . 1 ) c a n b e s o l v e d
f o r t h e i n t e r n a l r e a c t i o n r a t e s v e c t o r w h e n v a l u e s f o r
t h e p r i m a r y e x t e r n a l f l ow s a r e k n o w n . A s t h e s y s t e m i s
o v e r - d e t e r m i n e d b y o n e e q u a t i o n , f l o w s f o r g lu c o s e
a n d l y s i n e a r e s u f f i c ie n t to d o t h is . T h e s y s t e m w a s
s o l v e d f o r a ra n g e o f v a lu e s f o r t h e a p p a r e n t ( o v e r a ll )
l y s i n e y i e l d c o e f f i c i e n t Y p s, w h i c h i s t h e f l u x r a t i o
R p /
R s. F o r t h e b i o e n e r g e t i c p a r a m e t e r s a s e t o f r e a s o n a b l e
v a l u e s w a s a s s u m e d : t h e e f f i c i e n c y o f o x i d a t i v e p h o s -
p h o r y l a t i o n ( P / O r a t i o ) i s 1 . 5 , t h e b i o e n e r g e t i c g r o w t h
y i e l d Y A T P = 1 0 g / m o 1 A T P , a n d t h e e n e r g y c o s t s o f l y -
s i ne e x c r e t i o n a l = 1 m o l A T P / m o l l y si n e . T h e s e v a l u e s
r e s u l t i n a b i o m a s s y i e l d o n g l u c o s e o f 0 .5 0 g / m o l w h e n
n o l y s i n e p r o d u c t i o n t a k e s p l a c e , w h i c h c o r r e s p o n d s t o
v a l u e s n o r m a l l y f o u n d f o r h e t e r o t r o p h i c f u l l y r e s p i r a to -
r y m i c r o o r g a n i s m . M e t a b o l i c f l u x e s as a f u n c t i o n o f
~ p s
w e r e c a l c u l a t e d f o r v a r i o u s s e t s o f a l t e r n a t i v e r e a c t i o n s
t a k e n f r o m T a b l e 1 . T h e b a s ic s e t o f e q u a t i o n s i n c l u d es
t h e a l te r n a t i v e s i n d i c a t e d w i t h t h e l e tt e r a a d d e d t o
t h e i r r e a c t i o n n u m b e r .
F i g u r e 2 s h o w s t h e r e s u l t o f t h e m e t a b o l i c f l u x c a l c u -
l a t i o n f o r a n u m b e r o f r e l e v a n t r e a c t i o n s f o r t h e b a s ic
s e t o f e q u a t i o n s . F l u x e s a r e e x p r e s s e d i n m o l / h r e l a t i v e
t o t h e g l u c o s e f l u x , a n d a r e a l l l i n e a r f u n c t i o n s o f Y p s.
I t c a n b e s e e n th a t t h e f lu x t h r o u g h t h e H M P p a t h w a y
i n c r e a s e s w i t h t h e l y s i n e y i e l d , r e s p o n d i n g t o t h e i n -
c r e a s e d n e e d f o r r e d u c t i o n e q u i v a l e n t s i n t h e f o r m o f
N A D P H , w h i le s i m u l ta n e o u s ly t h e f lu x th r o u g h t h e
E m b d e n - M e y e r h o f p a t h w a y d e c r e as e s. T h i s c o r re l a t io n
b e t w e e n t h e f lu x t h r o u g h t h e H M P p a t h w a y a n d l y si n e
p r o d u c t i o n w a s s h o w n t o e x i s t e x p e r i m e n t a l l y b y Is h i n o
e t a l. ( 1 9 9 1) , u s in g a 1 3 C - N M R s t u d y . A t r e l a t i v e l y h i g h
v a l u e s o f
~ p s
t h e s t o i c h i o m e t r i c m o d e l e v e n p r e d i c t s a
X
k ~
1 ,5
1 .0
0 . 5
0 . 0
- 0 . 5
- 1 . 0
4
0 . 0 0 . 1 0 . 2 0 . 3 0 . 4 0 . 5 0 . 6 0 . 7
L y s i n e y i e l d M o l / M o l )
F/g. 2 Me tabolic fluxes for a range of overall lysine yields, calcu-
lated for the basic set of reactions from Table 1. Fluxes are ex-
pressed in mo l/h, relative to the glucose flux. Th e dark area of the
bar indicates the region of physiologically possible f luxes. 1
Em bden-M eyerhof pathway, 2 hexose monophosphate pathway,
3 citrate synthase, 4 succinyl-CoA synthase. Further details: see
text
r e v e rs i o n o f t h e f lu x t h ro u g h t h e E m b d e n - M e y e r h o f
p a t h w a y ( i. e. g lu c o s e 6 - p h o s p h a t e is p r o d u c e d f r o m
P - p y r u v a t e ) . T h i s i s a s i t u a t i o n w h e r e m o r e A T P i s
g e n e r a t e d i n l y s i n e b i o s y n t h e s i s t h a n c a n b e u s e d i n
b i o m a s s f o r m a t i o n . P h y s i o l o g i c a l l y s u c h a c o n d i t i o n i s
i m p o s s i b l e , b e c a u s e t h e p h o s p h o f r u c t o k i n a s e r e a c t i o n
i n t h e E m b d e n - M e y e r h o f p a t h w a y is i rr e ve r si b le . T h e
p o i n t w h e r e t h e f l u x t h r o u g h t h i s p a t h w a y b e c o m e s
z e r o r e p r e s e n t s , t h e r e f o r e , t h e m a x i m u m p o s s i b l e o v e r -
a ll y i e l d fo r l y s in e f o r m a t i o n u n d e r t h e a s s u m p t i o n t h a t
t h e b a s i c s e t o f m e t a b o l i c r e a c t i o n e q u a t i o n s i s v a l id .
T h e m a x i m u m y i e ld ( 0. 33 m o l / m o l ) , m i g h t b e e v e n l o w -
e r in p r a c ti c e , b e c a u s e i n t h e m o d e l n o N A D P H u t il iz a -
-
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1.5
1.0
2
513
1 . 0
0 . 5
X
m
ll
~
0
r~
0 5 -
0 . 0
X
0
0 . 0
- 0 . 5
_ 1 . 0 1 1
0 . 0 0 .1 0 . 2 0 . 3 0 . 4 0 . 5 0 . 6 0 . 7
L y s i n e y i e l d M o l / / M o l )
Fig. 3 Variation on Fig. 2: isocitrate dehydrogenase s NADP-de-
pendent. 1 Embden-Meyerhofpathway,2 hexose monophosphate
pathway, 3 citrate synthase, 4 succinyl-CoAsynthase. Further de-
tails: see text
- 0 . 5
- 1 . 0
0 . 0 0 . 1 0 . 2 0 . 3 0 . 4 0 . 5 0 . 6 0 . 7
L y s i n e y i e ld M o l / M o l )
Fig. 4 Variation on Fig. 2:glucose catabolism proceeds exclusive-
ly through the linear and cyclicvariants of the hexose monophos-
phate (HMP) pathway. 1 cyclic HMP pathway, 2 linear HMP
pathway, 3 citrate synthase,4 succinyl-CoAsynthase. Further de-
tails: see text
tion in biomass formation was assumed and, further-
more, it can be expected that metabolic problems will
occur when the flux through the Embden-Meyerhof
pathway is low but still not zero.
The dotted lines in Fig. 2 represent the flux through
the Embden- Meyerho f pathway calculated for two var-
iants of the basic set: the dehydrogenase variant of the
lysine biosynthesis pathway, which causes the line to
pass through zero at a lower value of
Y ps,
and the case
where ammonia is assimilated via the glutamine syn-
thase reaction, which shifts the limiting situation to a
higher Y ps value. Both variations on the basic set have
quantitatively irrelevant effects, and they will not be
discussed further.
The effect of cofactor preference of isocitrate dehy-
drogenase is shown in Fig. 3, which shows int ernal
fluxes assuming that isocitrate dehydrogenase exclu-
sively uses NAD P as cofactor. The general characteris-
tics remain the same, the critical yield being shifted to a
higher value. It can be seen that at low lysine yields
there is a surplus of NADPH formation, causing a re-
version of the HMP pathway, which is of course physi-
ologically impossible. It is also interesting to note the
reversion of the succinyl-CoA synthase reaction
at Y ps
values just below the maximum. Physiologically this
presents no problem because the reaction is reversible.
Finally, in Fig. 4 the hypothetica l occurrence of a cyclic
HMP pathway together with its linear variant is shown.
Only at high lysine yields is the NADPH requirement
large enough to cause a positive flux through the HMP
cycle. In this case the lysine yield will be limited by the
flux through the (irreversible) citrate synthase reaction,
which is calculated to become negative at very high
overall lysine yields.
Maximum possible overall yields for various meta-
bolic set-ups can be calculated by fixing the flux
through the critical reaction step (Embden-Meyerhof
pathway or citrate synthase) on a zero value, which de-
creases the degree of freedom of the system with one.
The matrix Z3 in the metabolic balance equation
(Eq. 5) then has the dimensions 2 x 3
n-m
= 2), which
allows the calculation of the fluxes R~ and
Rp
for a giv-
en value of Rs, resulting in fixed values for Y ps and
Y xs. Table 2 shows the results for a number of meta-
bolic variants. The table also contains values for the dif-
ferential yields corrected for glucose utilization for
growth (Yps
in Eq. 6).
The data in Table 2 are dependent on assumptions
about the bioenergetic parameters, Y TPand the P/O
ratio. It is therefore interesting to evaluate the effect of
variation of these parameters on the maximum possible
overall yield. This is done in Fig. 5 for the second meta-
bolic variant of Table 2. As could be expected, the fig-
ure shows that a low bioenergetic efficiency (either a
low P/O ratio or a low YATP s beneficial for the maxi-
mum possible overall lysine yield.
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514
3 0 0
2 2 5
I 5 0
0
0 7 5
0 0 0
5 0
7 5 1 0 0 1 2 5 1 5 0
Y a t p
Fig. 5 Contour lines for maximum possible overall lysine yields
as function of the efficiencyof oxidative phosphorylation
P/O
ratio) and the efficiencyof gro~vth (YATe)
iscussion
The differential yield of lysine on glucose appears to be
hardly influenced by the type of metabolism that is
used (Table 2). On first sight this seems surprising:
when the lysine biosynthesis reaction is considered in
isolation from the cellular metabolism, a yield of 1.0 is
calculated when oxaloacetate is formed through car-
boxylation of P-pyruva te, in comparison with a theore-
tical yield of 0.67 when the glyoxylate pathway is used
for this purpose. However, this difference in yield be-
comes much less when proper account is taken of the
substrate used for NADPH generation and the ATP
formed in the oxidation of excess NADH, using a meta-
bolic network equation of the form of Eq. 1. The differ-
ential yield of 0.78 mol/mol, calculated in case of the
P-pyruvate carboxylase reaction, is higher than the val-
ue of 0.69 mol/mol ment ioned in a study by Shvinka et
al. (1980). The difference can be explained by the fact
that these authors did not address the net energy pro-
duction in lysine biosynthesis, resulting in a saving in
the amount of glucose used for catabolic purposes.
The maximum conversion yield of lysine production
from glucose (when the lysine biosynthesis pathway
genes are sufficiently expressed) is shown to be limited
by over-production of energy, which causes the flux
through the glucose catabolic pathway to become zero.
This finding illustrates the value of metabolic flux anal-
ysis, not only for the assessment of the requ ired in vivo
activities of auxiliary pathways, but also as a tool to
identify limitation by reaction sequences that can not
run in a reverse direction. The estimated maximum
yield for at least a number of the metabolic variants
that were studied is lower than the highest yields for
lysine formation as reported in the literature. Appar-
ently, industrial strains use other pathways, or escape
mechanisms have been introduced during the process
of strain improvement (haphazardly or purposely). The
maximum lysine yield is quite sensitive to the way the
organism generates NADPH. When the hexose mono-
phosphat e rou te is the only possibility, a low maximum
yield of 0.33 mol/mol is calculated. Isocitrate dehydro-
genase generally occurs in two forms, a NAD-depend-
ent form and a NADP-dependent form. Normally it is
assumed that the isocitrate dehydrogenase reaction
uses NADP as a cofactor. However, if this were the
case an over-production of NADPH would result at
low lysine yields (Y ps
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