SlideShare a Scribd company logo
2
Most read
5
Most read
6
Most read
OTHER UNSTRUCTURED MODELS
Author: Guillermo Garibay Benítez University: Instituto Politécnico Nacional
Mexico
• Monod modified form:
• Shows initial concentration influence, which is
sometimes observed if others components are
growth limiting.
• Teisser equation
• Relates μ with S in a exponential manner.
• Gives same result as Monod model for low
values of S since e-s/k ≈ 1 – s/KS para S → 0, but
approximation to μm for large values of S is
generally very fast.
• Contois equation:
• Expresses saturation effective constant, this constant is
proportional to biomass concentration.
• At large values of X, μ is inversely proportional to X
• It is used in occasions to represent a diffusive limitation in
inmobilized biomass.
• Multiple substrate monod kinetics
• Any substrate can be growth limiting, under
conditions when another substrate is in excess.
• Para S1=K1 y S2=K2, μ=μm/4
• An example is simultaneous requirement of
glucose and oxigen by aerobic organisms.
 Double Monod kinetics
 It can be described for two substrates acting like parallel
reactions.
 Each substrate allows a different maximum specific growth
rate
 It is used, for example, in the usage of alternative
substrates like different types of sugars.
• Monod Diauxic growht
• It can be modelled for two substrates
• In this manner, S2 substrate uptake will be
inhibited until S1 finishes, for low values of KI
• Product inhibition
• Inhibitory effect of lactic acid. Bibal et al (1988) studied the inhibiton of
lactic acid on Streptococcus cremoris.
• This influence was examined measuring specific growth rate during batch
growth of the bacterium in media containing various concentrations of
lactic acid (p). The results are summarized below:
• It is mainly the dissociated form of lactic acid that passes through the
cellular membrane, and we will therefore assume that it is only the
undissociated acid that has a toxic effect on the cells. Plot the relative
specific growth rate, i.e. µmax(p)/µmax(p=0), versus the concentration of
undissociated acid concentration (in mM). pH = 6.3 was used and pKa for
lactic acid is 3.88. Assume the first inhibition model mentioned above
holds. Find the inhibition constant Ki. Plot the model with the experiments
p (g /L) µ(h-1)
0 0.90
12 0.68
39 0.52
55 0.13
Continuation…
• There seems to be a certain maximum
concentration of undissociated acid above
which growth stops. Try the next model to find
the influence of pu on µ and estimate the
model parameter. At what concentration of
lactic acid will growth stop?
• An hybridome cell line is used for production of monoclonal
antibodies. In a batch growth, the following data was
obtained:
Time (days) Cell concentration
(cells mL-1x10-6)
0 0.45
0.2 0.52
0.5 0.65
1 0.81
1.5 1.22
2 1.77
2.5 2.13
3 3.55
3.5 4.02
4 3.77
4.5 2.2
Calculate specific growth
rate during growth fase and
duplication time
Other unstructured growth models slideshare

More Related Content

PPT
immobilized Enzyme reactors- batch and continuous types.
PPTX
Bacterial growth curve monods equation
PDF
Continuous stirred tank reactor (CSTR )
PPTX
unstructured growth kinetics
PPTX
Unstructured model on population level
PPTX
Solid liquid separation - unit operations
PPTX
Lecture 3 bioprocess control
PPTX
Trickle bed reactor
immobilized Enzyme reactors- batch and continuous types.
Bacterial growth curve monods equation
Continuous stirred tank reactor (CSTR )
unstructured growth kinetics
Unstructured model on population level
Solid liquid separation - unit operations
Lecture 3 bioprocess control
Trickle bed reactor

What's hot (20)

PPTX
Cellular Growth Modelling and Classification
PDF
Automated DNA sequencing ; Protein sequencing
PPT
Acetone butanol production
PPTX
Dialysis
PPTX
Bioreactors
PPTX
Chapter 1 mass balance series of lecture of bioprocess engineering
PDF
Measurement of mass transfer coefficient (k la)
PPTX
Inocula development for yeast processes
PPTX
Air and media sterilisation
PPTX
Bioreactor control system
PPT
Aqueous two phase extraction
PPTX
Bubble column reactor
PDF
synthesis of nanoparticles using microbes
PPTX
Animal cell, tissue culture
PPTX
Microbial growth kinetcs
PPTX
Sedimentation for determining molecular weight of macromolecules
PPT
Development of inoculum buildup
PPTX
Downstream Processing
PPTX
Ligase Chain Reaction(LCR)
PPTX
B.Sc. Microbiology II Bacteriology Unit 4.3 Types of Culture
Cellular Growth Modelling and Classification
Automated DNA sequencing ; Protein sequencing
Acetone butanol production
Dialysis
Bioreactors
Chapter 1 mass balance series of lecture of bioprocess engineering
Measurement of mass transfer coefficient (k la)
Inocula development for yeast processes
Air and media sterilisation
Bioreactor control system
Aqueous two phase extraction
Bubble column reactor
synthesis of nanoparticles using microbes
Animal cell, tissue culture
Microbial growth kinetcs
Sedimentation for determining molecular weight of macromolecules
Development of inoculum buildup
Downstream Processing
Ligase Chain Reaction(LCR)
B.Sc. Microbiology II Bacteriology Unit 4.3 Types of Culture
Ad

Similar to Other unstructured growth models slideshare (8)

PPTX
ch9 for bioprocess - cell growth kinetics
PPTX
21BTC204 -UNIT II - FINAL.pptxbjrkjekrenhf
PPT
1919hghggghhdfdrghjfgffddrdrd49-6919.ppt
PPT
Growth kinetics derivation
PPTX
Growth kinetics
PPTX
Seminar MB.pptx
PPTX
Topic 1.Microbial growth curves and culture systems (2).pptx
PPT
Kinetics of growth
ch9 for bioprocess - cell growth kinetics
21BTC204 -UNIT II - FINAL.pptxbjrkjekrenhf
1919hghggghhdfdrghjfgffddrdrd49-6919.ppt
Growth kinetics derivation
Growth kinetics
Seminar MB.pptx
Topic 1.Microbial growth curves and culture systems (2).pptx
Kinetics of growth
Ad

More from Guillermo Garibay (16)

PPTX
2 desarrollo histórico de los productos biológicos
PPTX
stoichiometry of cellular reactions
PPTX
balances elementales
PPTX
Metabolic heat production
PPTX
Modelos cinéticos estructurados
PPTX
1 Curso Ingeniería Celular
PPTX
Generación de transfectomas
PPTX
Medición de flujo
PPTX
Medición de nivel
PPTX
Filtración
PPTX
Extracción bifásica
PPTX
Precipitación
PPTX
Separación por membranas
PPTX
Disrupción celular
PPTX
Teoría de la centrifugación
PPTX
Generalidades Centrifugación
2 desarrollo histórico de los productos biológicos
stoichiometry of cellular reactions
balances elementales
Metabolic heat production
Modelos cinéticos estructurados
1 Curso Ingeniería Celular
Generación de transfectomas
Medición de flujo
Medición de nivel
Filtración
Extracción bifásica
Precipitación
Separación por membranas
Disrupción celular
Teoría de la centrifugación
Generalidades Centrifugación

Recently uploaded (20)

PDF
COURSE DESCRIPTOR OF SURVEYING R24 SYLLABUS
PDF
86236642-Electric-Loco-Shed.pdf jfkduklg
PDF
Exploratory_Data_Analysis_Fundamentals.pdf
PPTX
introduction to high performance computing
PDF
PPT on Performance Review to get promotions
PPTX
Information Storage and Retrieval Techniques Unit III
PDF
PREDICTION OF DIABETES FROM ELECTRONIC HEALTH RECORDS
PDF
Unit I ESSENTIAL OF DIGITAL MARKETING.pdf
PDF
Visual Aids for Exploratory Data Analysis.pdf
PDF
A SYSTEMATIC REVIEW OF APPLICATIONS IN FRAUD DETECTION
PPTX
Artificial Intelligence
PPT
introduction to datamining and warehousing
PDF
The CXO Playbook 2025 – Future-Ready Strategies for C-Suite Leaders Cerebrai...
PDF
Enhancing Cyber Defense Against Zero-Day Attacks using Ensemble Neural Networks
PDF
III.4.1.2_The_Space_Environment.p pdffdf
PDF
Automation-in-Manufacturing-Chapter-Introduction.pdf
PPTX
CURRICULAM DESIGN engineering FOR CSE 2025.pptx
PPTX
UNIT 4 Total Quality Management .pptx
PPTX
UNIT - 3 Total quality Management .pptx
PPT
A5_DistSysCh1.ppt_INTRODUCTION TO DISTRIBUTED SYSTEMS
COURSE DESCRIPTOR OF SURVEYING R24 SYLLABUS
86236642-Electric-Loco-Shed.pdf jfkduklg
Exploratory_Data_Analysis_Fundamentals.pdf
introduction to high performance computing
PPT on Performance Review to get promotions
Information Storage and Retrieval Techniques Unit III
PREDICTION OF DIABETES FROM ELECTRONIC HEALTH RECORDS
Unit I ESSENTIAL OF DIGITAL MARKETING.pdf
Visual Aids for Exploratory Data Analysis.pdf
A SYSTEMATIC REVIEW OF APPLICATIONS IN FRAUD DETECTION
Artificial Intelligence
introduction to datamining and warehousing
The CXO Playbook 2025 – Future-Ready Strategies for C-Suite Leaders Cerebrai...
Enhancing Cyber Defense Against Zero-Day Attacks using Ensemble Neural Networks
III.4.1.2_The_Space_Environment.p pdffdf
Automation-in-Manufacturing-Chapter-Introduction.pdf
CURRICULAM DESIGN engineering FOR CSE 2025.pptx
UNIT 4 Total Quality Management .pptx
UNIT - 3 Total quality Management .pptx
A5_DistSysCh1.ppt_INTRODUCTION TO DISTRIBUTED SYSTEMS

Other unstructured growth models slideshare

  • 1. OTHER UNSTRUCTURED MODELS Author: Guillermo Garibay Benítez University: Instituto Politécnico Nacional Mexico
  • 2. • Monod modified form: • Shows initial concentration influence, which is sometimes observed if others components are growth limiting.
  • 3. • Teisser equation • Relates μ with S in a exponential manner. • Gives same result as Monod model for low values of S since e-s/k ≈ 1 – s/KS para S → 0, but approximation to μm for large values of S is generally very fast.
  • 4. • Contois equation: • Expresses saturation effective constant, this constant is proportional to biomass concentration. • At large values of X, μ is inversely proportional to X • It is used in occasions to represent a diffusive limitation in inmobilized biomass.
  • 5. • Multiple substrate monod kinetics • Any substrate can be growth limiting, under conditions when another substrate is in excess. • Para S1=K1 y S2=K2, μ=μm/4 • An example is simultaneous requirement of glucose and oxigen by aerobic organisms.
  • 6.  Double Monod kinetics  It can be described for two substrates acting like parallel reactions.  Each substrate allows a different maximum specific growth rate  It is used, for example, in the usage of alternative substrates like different types of sugars.
  • 7. • Monod Diauxic growht • It can be modelled for two substrates • In this manner, S2 substrate uptake will be inhibited until S1 finishes, for low values of KI
  • 9. • Inhibitory effect of lactic acid. Bibal et al (1988) studied the inhibiton of lactic acid on Streptococcus cremoris. • This influence was examined measuring specific growth rate during batch growth of the bacterium in media containing various concentrations of lactic acid (p). The results are summarized below: • It is mainly the dissociated form of lactic acid that passes through the cellular membrane, and we will therefore assume that it is only the undissociated acid that has a toxic effect on the cells. Plot the relative specific growth rate, i.e. µmax(p)/µmax(p=0), versus the concentration of undissociated acid concentration (in mM). pH = 6.3 was used and pKa for lactic acid is 3.88. Assume the first inhibition model mentioned above holds. Find the inhibition constant Ki. Plot the model with the experiments p (g /L) µ(h-1) 0 0.90 12 0.68 39 0.52 55 0.13
  • 10. Continuation… • There seems to be a certain maximum concentration of undissociated acid above which growth stops. Try the next model to find the influence of pu on µ and estimate the model parameter. At what concentration of lactic acid will growth stop?
  • 11. • An hybridome cell line is used for production of monoclonal antibodies. In a batch growth, the following data was obtained: Time (days) Cell concentration (cells mL-1x10-6) 0 0.45 0.2 0.52 0.5 0.65 1 0.81 1.5 1.22 2 1.77 2.5 2.13 3 3.55 3.5 4.02 4 3.77 4.5 2.2 Calculate specific growth rate during growth fase and duplication time

Editor's Notes

  • #12: u=0.67 d-1 Td=ln2/u = 1 d