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MiniCourse on Mathematical Modeling of Biological Systems

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ui = fraction critical resources. Instantaneous optimization. ui = maximizes return ... process: 'green' synthesis route for polyesters. Potential applications ... – PowerPoint PPT presentation

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Title: MiniCourse on Mathematical Modeling of Biological Systems


1
Mini-Course onMathematical Modeling of
Biological Systems
  • Frank Doyle
  • Dept. of Chemical Engineering
  • University of Delaware
  • (302) 831-0760
  • fdoyle_at_udel.edu

2
General Descriptions of Metabolic Systems
  • In general, dynamics must be accounted for
  • A number of simplifying assumptions invoked
  • steady-state
  • simple goals or costs functions

3
Cybernetic Models
  • Introduced by Ramkrishna co-workers
  • Key tenet microorganisms implement regulatory
    strategies with outcomes consistent with a
    desired goal
  • Requires formulation of objective function for
    specific structural units from which cybernetic
    control variables are defined (enzyme synthesis
    enzyme activity)
  • Does not replace detailed modeling of metabolic
    pathways or ignore biochemical details - rather
    it supplies the regulatory mechanisms
  • Wide success in describing varying bacterial
    uptake patterns of mixed, substitutable
    substrates in batch, fed-batch, and continuous
    reactors

4
Basic Postulates
  • The primary goal of a microorganism is to
    maximize growth rate.
  • The objective of promoting any irreversible
    linear pathway is the maximization of that
    pathways end product.
  • All end products produced at a branch point are
    essential for growth therefore cellular growth
    stops when any one end product is absent.
  • The objective of promoting any irreversible
    branched pathway is the maximization of the
    mathematical product of the end products produced
    by one or more branch points.
  • The objective of promoting any irreversible
    cyclic pathway is the maximization of the
    mathematical product of all the intermediates of
    the cycle whether or not they were withdrawn for
    further utilization in order to maintain the
    integrity of the cycle.

5
(contd)
  • In the presence of competing processes, whether
    substitutable or complementary in nature, the
    enzyme catalyzing the process that provides for
    the greatest return will be activated to the
    greatest extent. The appropriate measure of the
    returns received from promoting a given process
    is dependent upon the process type, e.g.,
    substitutable or complementary.
  • Metabolic regulation is present in a hierarchical
    structure compromising both local and global
    levels
  • As the status of a substrate is altered form
    limiting to nonlimiting, the excess substrate is
    available for the synthesis of additional
    structural and energetic resources.

6
Cybernetic Framework
BIOMASS
ENZYMES
INTERNAL RESOURCES INTERMEDIATES
C
N
ENZYME SYNTHESIS
REGULATORY PROCESSES
S
P
METABOLISM (INTERMEDIATE SYNTHESIS)
etc.
O
7
Optimal Control vs. Instantaneous Optimization
  • Endpoint optimization
  • ui fraction critical resources
  • Instantaneous optimization
  • ui maximizes return

8
Example Klebsiella pneumoniae
  • glucose feed, watch cell density as output
  • Model equations
  • cell density
  • growth enzyme
  • maintenance enzyme
  • cellular resource level
  • substrate concentration

9
Key Rate Functions
  • growth rate
  • growth enzyme production rate
  • maintenance enzyme production rate
  • rate of resource synthesis

10
PHB production in Alcaligenes eutrophus
  • Motivation
  • polymer biodegradable, thermoplastic
  • process green synthesis route for polyesters
  • Potential applications
  • medical (implants, drug delivery)
  • film, packaging
  • Cybernetic model developed by Varner Bailey

11
Pathway Structure
  • p3 PHB

storage pathway model
cr
example cybernetic variable governing synthesis
of key biomass growth enzyme, eg
12
Cybernetic Variable Governing Synthesis of Key
Growth Enzyme
Cybernetic variable adjusting synthesis rate of eg
Ammonium nitrate concentration in reactor
13
Model Equations
14
Parameter Identification
  • Model parameters identified from batch cultures

15
Continuous Culture with Biomass Recycle
biomass recycle
dilution rate (glucose and ammonium feed)
PHB productivity
ideal separator (microfiltration)
reactor
glucose measurement
16
Wash-out Disturbance
17
Cybernetic Variable Profiles
  • Cybernetic variables governing synthesis of
    enzymes for PHB storage and biomass growth

18
Cybernetic Variables Governing Enzyme Activity
  • Cybernetic variables are non-smooth functions
  • cybernetic variable modulating activity of
    storage enzyme
  • Batch culture profile for v3
  • Gradient based optimization?

19
Generalized Framework (Varner, 2000)
20
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