Basic rules of microbial growth Basic rules of microbial growth
Fermentation up stream and down stream processes
E.coli Vibrio cholerae
Saccharomyces cerevisiae
Mucor circenelloides Aszexuális gombanövekedés
Basic rules of microbial growth Basic rules of microbial growth
1=X0*20
2=X0*21
4=X0*22
n=1
n=2
n=3
Binary dividing microorganisms
8=X0*23
16=X0*24
n=3
n=4
n:no of new generations
. .
X=X02n
t g
n = t No of generations
Generációs idő - doubling time generation time
N, x
Cell number pc/ml
Cell mass: dw mg/ml, g/l,kg/m3
Basic rules of microbial growth Basic rules of microbial growth
n 0
t t
0 2 x 2
x
x =
g=
MONOD, 1942x dt .
dx = µ
µ: specific growth rate
x dt .
dx = µ
Specific growth rate
Basic rules of microbial growth Basic rules of microbial growth
dt dx x
≡ 1
µ h
-1x dt .
dx = µ . N
dt
dN = ν
e t
x
x = µ N = N e ν t
Jacques Monod
Basic rules of microbial growth Basic rules of microbial growth
Specific proliferation rate Spec. Doubling rate
t 0 e x
x = µ N = N 0 e ν t
Relation between µ and tg:
= ln µ 2
t
gx ∞
t 0 e x
x = µ
Basic rules of microbial growth Basic rules of microbial growth
t
In reality
x
0x
LAG
PHASE
ACCELERA TING
GROWTH
EXPONEN- TIAL
PHASE
Basic rules of microbial growth Basic rules of microbial growth
x
0t
PHASE
GROWTH
PHASE DECLINING PHASE
x
0t dx
x x
g
maxcot α = µ
Basic rules of microbial growth Basic rules of microbial growth
µ t
t
dt
dx
WHAT IS THE REASON OF THE EXISTENCE OD DECLINING PHASE?
1. NUTRIENT LIMITATION
2. TOXIC METABOLIT PRODUCT(S) 3. LACK OF SPACE
MONOD- model
µ µ
maxBasic rules of microbial growth Basic rules of microbial growth
S K
S
S
max +
µ
=
µ µ
max2
Κ
SS
CRITICALS
KRITICAL SUBSTRATE CONCENTRATION LIMITING SUBSTRATE
µ µ
maxΚ
SNS
krNS
0NN-source
~ ~
µ µ
maxΚ
SCS
krCS
0CC-Source
~ ~
FERM.TIME FERM.TIME
WHICH S WILL BE LIMITING
???
Basic rules of microbial growth Basic rules of microbial growth
NOTION OF THE LIMITING SUBSTRATE
µ
maxµ µ
maxΚ
SVS
krVS
0VVITAMINe -source
~ ~
µ
Κ
SOS
krOS
0OO
2~ ~
Κ
SS
krNS
0NΚ
SS
krS
0FERM.TIME
FERM.TIME
tgα=KS/µmax
1/ µ
1/S 1/µ
maxLINEWEAVER-BURK
tgα=1/µmax
S/ µ
K
S/ µ
maxHANES v. LANGMUIR
S K
S S
µ µ= +µ max max
1 *
1 1 1
µ µ = + µ
max max Ks * S
Basic rules of microbial growth Basic rules of microbial growth
-1/K
S1/S K
SS
µ
µ /S µ
maxtg α =-K
Sµ
max/K
Sµ µ = max KS − µ S
EADIE-HOFSTEE
dt dS x
1 dt dx x
1 S
x dS Y
dx
s /
x
=
∆
= ∆
−
=
dx = µ
=
YIELD COEFF:
i s
/ x i
-Y
vagy
dS Y dx
i
=
−
=
FOR THE LIMITING S
EXTENSION
Basic rules of microbial growth Basic rules of microbial growth
dt x
r
x= dx = µ
S x K
S Y
1 dt
r dS
S x K
S dt
r dx
S S
/ x S
S x
µ +
−
=
=
µ +
=
=
ALWAYS TRUE:
In the exponential and declining phase:
MONOD-model
Differential equation Can be solved
x
x
µ Y vagy -Y dt µ
dx
∆x
dx = = = = − =
Basic rules of microbial growth Basic rules of microbial growth
i x/s
S x S
x i
-Y vagy
Q Y µ µ
µ dt
dS dt
∆S
∆x dS
dx
i
=
−
=
=
=
=
Utilization of C/en source
S S
S = ∆
C+ ∆
E∆
∆ S = ∆ S c + ∆ S E
What for?
incorporation energy production
Basic rules of microbial growth Basic rules of microbial growth
x x
x
E C
+ ∆
= ∆
∆
Yield of incorp. carbon Energy yield Overall yield
Y Y
YY Y
1 Y
1 Y 1
C C
C
E
= −
= −
Y 1 Y
1 Y
1
E C
x/s
+
=
=
2 ∆ x
α α
1∆ S
CC-content of the cell mass C-content of the substráate 0,46-0,5 50%
2 1 C
c
S Y x
α
= α
∆ =
∆
Glucose:0,4Material balance for the incorporated carbon
Basic rules of microbial growth Basic rules of microbial growth
2
S
cα
∆
2 1
1
2 1
2 1
E
Y .
. Y Y
. Y
Y α − α
= α α −
α α α
=
Some cases from the product one can estimate the energy production and consumption
Assimilated Dissimilated EtOH yeast, sugar
AcOH A.aceti, alcohol
NADH !!!
Glükonsav A.suboxydans, glucose
Basic rules of microbial growth Basic rules of microbial growth
Assimilated Dissimilated
Strain cult. media ratio of cult. media
% %
Streptococcus faecalis
anaerobic growth complett 2 98 Saccharomyces cerevisiae complett
aerobic growth 10 90
anaerobic growth 2 98
Aerobacter cloaceae minimal 55 45
1,2,3,
∆ S = ∆ S c + ∆ S E
?
Cell growth Maintenance of viability Cell motion
Osmotic work
Basic rules of microbial growth Basic rules of microbial growth
Osmotic work
Mantenance of orderness
thermodynamics II.law resyntheses
Y x
S
x
S S
E
E g m
= =
+
∆
∆
∆
∆ ∆
dS
dt Y
dx dt
x
= − 1 = − µ Y
dt dS dt
dS Y
dt
dS
g mE x E
+ µ =
=
dS dt
x Y
g = µ dS
dt m = mx
1 1
Y Y
m
E EG
= +
µ
!!!
Basic rules of microbial growth Basic rules of microbial growth
dt = Y EG
dt = mx
µ x µ Y
x
Y mx
E EG
= +
1 1
Y Y
m
E EG
= +
µ
modell
1 1
Y Y
m
E EG
= +
µ
specific maintenance coefficient
g/gh =h
-11 1 1
Y Y Y
m
x s / c EG
= + +
µ
For the overall yield:
1
Basic rules of microbial growth Basic rules of microbial growth
Y x s / Y c Y EG µ
m µ 1 1
Y
c+ Y
EG1 Y
x s/1
µ m
1 1
Y
c+ Y
EGS s
/
Y µ
x= µ
m
µ
Y 1 Y
1
EG C
S µ+
+
= µ
ATP-yield
Y x ATP
Y
ATP
Y
x s ATP s
= ∆ = ′
∆
/ /
′ =
Y
x s/MY
x s/g/mol
g/mol
mol/mol
( ) ( )
m Y
1 Y
1
ATP ATP
ATP
ATP max
ATP ATP
m g
+ µ
=
∆ +
∆
=
∆
10,5 g/mol
Q
ATPY Y m
ATP ATP
= µ = µ +
ATP max(8,3-32)
Basic rules of microbial growth Basic rules of microbial growth
culture specific mentenance
conditions coefficients
m mATP Aerobacter cloaceae aerobic, glucose 0,094 14 Saccharomyces cerevisiae anaerobic glucose 0,036 0,52
+ 0,1 mol/dm3 NaCl Saccharomyces cerevisiae anaerobic, glucose
+1,0 mol/dm3 NaCl 0,360 2,2 Penicillium chrysogenum aerobic 0.,022 3,2 Lactobacillus casei aeroic, glucose 0,135 1,5
O
P
Effectivity of oxidatíve phosphorilation„P/O ratio”
mol/gatom
NADH + H+ + 1/2O2 + 3 ADP + 3 H3PO4 NAD+ + 3 ATP + 4 H2O
3/1=3
Basic rules of microbial growth Basic rules of microbial growth
x Y P
S
Y P
x p s
p
∆
= ∆
∆
= ∆
Q x S
. H x
. H Y x
Y
S x
kcal
H
∆
= ∆
∆
∆ +
∆
∆
−
= ∆
=
HEAT PROD. YIELD ENTHALPY OF
CELL MASS
ENTHALPY OF SUBSTRATE
METABOLIC
HEAT PRODUCTION
Basic rules of microbial growth Basic rules of microbial growth
HEAT PROD. YIELD
CELL MASS
x x/S
S
x/S S
x kcal
H
∆H Y ∆H
Y .∆∆S/∆
∆H x/ ∆/
.
∆H
∆x/∆S Y
Y = −
+
∆
= −
=
IF THERE IS NO SIGNIFICANT EXTRACELLULAR PRODUCTION
RQ respiration quotient
2 2
O CO 2
2
2 2
q q dt
dO dt dCO O
CO = =
∆
∆
Basic rules of microbial growth Basic rules of microbial growth
C
6H
12O
6+ 6O
26CO
2+ 6 H
2O
RQmax = 12C2H5OH + 6 O2 4 CO2 + 6 H2O RQmax =4/6= 0,67
C
6H
12O
6 C2H5OH+ CO
22 CH3OH + 3 O2 2 CO2 + 4H2O C2H2O4 + ½ O2 2CO2 + H2O
RQmax =
RQmax =2/3= 0,67 RQmax =2/ ½ = 4
∞
x x
P P x P
GAEDEN:production types
Primary products Secondary products
Growth associated Mixed type Non growth associated
µ
xµ
xµ
xµ
Pµ
Pµ
PKINETICS OF PRODUCT FORMATION
LUEDEKING – PIRET MODEL r dP
dt
dx
dt x x
dP dt
P
P x
= = +
= = +
α β
µ αµ β
1
µP
tgφ=α
III.
µX β
tgφ=α φ
φ β