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6 3 Quantifying Growth Kinetics 6.3. Quantifying Growth Kinetics Model Model Unstructured Structured . N Most idealized case Cell population treated as Multicomponent Nonsegr Balanced Growth one component solute average cell description regated (approximation) Average cell Average cell single component Multicomponent Seg Balanced approximation approximation heterogeneous description of cell-to-cell individual cells heterogeneity gregated Growth (approximation) Actual case d .

6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

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Page 1: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kinetics

ModelModelUnstructured Structured .N

Most idealized caseCell population treated as Multicomponent

Nonsegr

BalancedGrowth

one component solute average cell description

regated

(approximation)Average cell Average cell

single component Multicomponent

Seg Balanced

approximation approximation

g p pheterogeneous description of cell-to-cellindividual cells heterogeneity

gregated

Growth

(approximation)Actual case

d .

Page 2: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

6.3.2. Using Unstructured Nonsegregated Modelsto Predict Specific Growth Rate

6 3 2 1 Substrate-limited growth6.3.2.1. Substrate-limited growth

Monod equationMonod equation

µ =µm S_____ µ Ks + S

µm : maximum specific growth rateKs : saturation constant

Other equations

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Other equationsfor substrate-limited growth

Page 4: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

When more than one substrate is growth rate limiting

Interactive or multiplicativeµ/µ = [µ(s )] [µ(s )] [µ(s )]µ/µm = [µ(s1)] [µ(s2)] … [µ(sn)]

AdditiveAdditiveµ/µm = w1 [µ(s1)] + w2 [µ(s2)] + … + wN [µ(sn)]

Noninteractive( ) ( ) ( )µ = µ(s1) or µ(s2) or … µ(sn)where the lowest value of µ(si) is used.µ( i)

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6 3 2 2 Models with growth inhibitors6.3.2.2. Models with growth inhibitors

The inhibition pattern of microbial growth is analogous to enzyme inhibition.a a ogous to e y e b t o

Substrate inhibition

Product inhibition

Inhibition by toxic compound

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Substrate Inhibitionof Cell Growth

Page 7: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

Enzyme InhibitionEnzyme Inhibition

N titi i hibitiNoncompetitive inhibition

Competitive inhibition

Page 8: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

Product Inhibition of Cell GrowthProduct Inhibition of Cell Growth

Page 9: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

Cell Growth in Ethanol FermentationCell Growth in Ethanol Fermentation

Page 10: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

Inhibition by Toxic CompoundsInhibition by Toxic Compounds

Page 11: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

Enzyme InhibitionEnzyme Inhibition

Competitive inhibitionCompetitive inhibition

Noncompetitive inhibitionNoncompetitive inhibition

Page 12: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

Enzyme InhibitionEnzyme Inhibition

Uncompetitive inhibition

Page 13: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

Inhibition by Toxic CompoundsInhibition by Toxic Compounds

Page 14: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

6 3 2 3 The logistic equation6.3.2.3. The logistic equation

dX/dt XdX/dt = µ X

dX/dt k (1 X/X ) X X(0) XdX/dt = k (1-X/X∞) X, X(0)=X0

X0 ektX =

X0 e1- (X0 /X∞) (1 - ekt)

______________

Sigmoidal(stationary phase involved)

Page 15: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

6.3.2.4. Growth modelfor filamentous organisms

In suspension culture : formation of microbial pelletOn solid medium : colony (long and highly branched cellsy ( g g y

In the absence of mass transfer limitations

R∝ t R: radius of a microbial pelletR t R: radius of a microbial pelletradius of a mold colony

dR/dt = kp = constant Eq(1)

Page 16: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

Growth model for filamentous organismsGrowth model for filamentous organisms

M : mass of pellet

dM/dt (4 R2) (dR/dt)dM/dt = ρ (4πR2) (dR/dt)

= kp ρ (4πR2) (by Eq(1))p ρ ( ) ( y q( ))

= kp (36πρ)1/3 (4/3 πR3ρ)2/3

= γ M2/3 Eq(2)

where γ = kp (36πρ)1/3

M = 4/3 πR3ρ

Page 17: 6 3 Quantifying Growth Kinetics6.3. Quantifying Growth Kineticsocw.snu.ac.kr/sites/default/files/NOTE/5593.pdf · 2018. 1. 30. · 6.3.2. Using Unstructured Nonsegregated Models to

Growth model for filamentous organismsGrowth model for filamentous organisms

E (2)Eq(2)

dM/dt = γ M2/3 Eq(2)γ q( )

M-2/3 dM = γ dt

3 [M1/3] = γ t

M = (M 1/3 + (γ t)/3)3

M

M0

M = (M01/3 + (γ t)/3)3

≈ (γ t /3)3

M0 (the initial biomass) is usually very smallcompared to Mcompared to M.

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6 3 3 Chemically Structured Model6.3.3. Chemically Structured Model

Since it is not practical to write material balances on every cell component, we must select skillfully the key variables and processes of major interest in a particular application when formulating aof major interest in a particular application when formulating a structured kinetic model.

Mass balance inside the cell

Batch VR : total volume of liquid in the reactorC : extrinsic concentration of component iCi : extrinsic concentration of component iX : extrinsic concentration of biomass

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Intrinsic and Extrinsic ConcentrationsIntrinsic and Extrinsic Concentrations

Intrinsic concentrationThe amount of a compound per unit cell mass (or cellThe amount of a compound per unit cell mass (or cell volume)

Extrinsic concentrationThe amount of a compound per unit reactor volumeThe amount of a compound per unit reactor volume

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Intrinsic and Extrinsic ConcentrationsIntrinsic and Extrinsic Concentrations

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Intrinsic and Extrinsic ConcentrationsIntrinsic and Extrinsic Concentrations

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Single-cell model for E. coli by Shuler and colleagues

Fig. 6.14

The model contains the order of 100 stoichiometric and kinetic parameters almost allstoichiometric and kinetic parameters, almost all of which can be determined from previous literature an the biochemistry of E coli growthliterature an the biochemistry of E. coli growth.

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Single-cell model for E. coli by Shuler and colleagues