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Modeling Chassis Induction Chitin Apoptosis


The main purpose of modeling was to characterize the topography of the kinetics behind foreign protein/product production in recombinant E.Coli biofilm with a diffusing inducer, and the effect on the various species involved by primarily the following factors:

  • Time-derivative Spatial-Gradient Inducer Concentration
  • Repressor Concentration
  • Ribosome Binding Site (Rate of Transcription)

In terms of our iGEM project, this model was employed to explore the effect of IPTG concentration and diffusion, lacI concentration (determined by the combination part of constitutive promoter, ribosome binding site, lacI gene, double terminator, lac promoter/operon), and the ribosome binding site on the concentrations of all species involved - described in the following sections - and especially on Chitin Synthase and Chitin concentration and the corresponding rates.


Overall Model

Using enzyme kinetics equations, we elected to mathematically simulate the following model:



Iex: External Inducer, determined by diffusion through Fick's law (IPTG in our experiment)

Iin: Internal Inducer (IPTG)

Ii: Inducer bound to Repressor (IPTG bound to lacI)

i: Repressor (lacI)

Db: Repressor-bound DNA (lacI-bound DNA(CHS3) region in plasmid)

Dunb: transcribe-able or Repressor-unbound DNA (lacI-unbound DNA(CHS3))

Re: mRNA for Enzyme (CHS3 mRNA)

E: Enzyme (CHS3)

S: Substrate (N-Acetyl Glucosamine)

C: Enzyme Substrate Complex (CHS3-(N-Acetyl-Glucosamine)-Chitin or (NAG)n Complex)

P: Protein Product (Chitin or (NAG)n+1)


The differential of the variables were found as follows:

  • dIin = kIin*Iex - kIex*Iin + kIir*Ii - kIif*Iin*i
  • dIi = kIif*Iin*i - kIir*Ii
  • di = kIir*Ii - kIif*Iin*i + kDbr*Db - kDbf*i*Dunb
  • dDb = kDbf*i*Dunb - kDbr*Db
  • dDunb = kDbr*Db - kDbf*i*Dunb
  • dRe = ktscribe*Dunb - kRdeg*Re
  • dE = ktslate*Re - kEdeg*E + kCr*CC + kP*CC - kCf*E*Si
  • dSi = ksin*So - kCf*E*Si + kCr*CC;
  • dCC = kCf*E*Si - kCr*CC - kP*CC;
  • dP = kP*CC - kPdeg*P;

IPTG Diffusion

First, Fick's Law of Diffusion was modeled through MATLAB. The diffusion constant used was 220um^2/s.[4]


IPTG is sprayed at the top of the colony, which then diffuses as according to Fick's law. The spatial local concentration will then differentially induce downstream processes.

Semi-Empirical Determination

Fitted Model

Matlab was used to generate a theoretical model where IPTG would diffuse down the biofilm as according to Fick's Law of Diffusion and initiate the process. The extracellular substrate concentration was assumed to be much greater than the uptake/use, and so would diffuse in at a constant rate.

This model was fitted with empirical data using cp-lacpi-gfp to estimate the rate constant, and therefore the effects of varying cp, lacpi, and rbs on enzyme and final product production.


1. A novel structured kinetic modeling approach for the analysis of plasmid instability in recombinant bacterial cultures

William E. Bentley, Dhinakar S. Kompala Article first published online: 18 FEB 2004 DOI: 10.1002/bit.260330108

2. Mathematical modeling of induced foreign protein production by recombinant bacteria

Jongdae Lee, W. Fred Ramirez Article first published online: 19 FEB 2004 DOI: 10.1002/bit.260390608

3. Pool Levels of UDP N-Acetylglucosamine and UDP NAcetylglucosamine-Enolpyruvate in Escherichia coli and Correlation with Peptidoglycan Synthesis

DOMINIQUE MENGIN-LECREULX, BERNARD FLOURET, AND JEAN VAN HEIJENOORT* E.R. 245 du C.N.R.S., Institut de Biochimie, Universit' Paris-Sud, Orsay, 91405, France Received 9 February 1983/Accepted 15 March 1983

4. Diffusion in Biofilms

Philip S. Stewart Center for Biofilm Engineering and Department of Chemical Engineering, Montana State University–Bozeman, Bozeman, Montana, 59717-3980

5. Regulation of the Synthesis of the Lactose Repressor

PATRICIA L. EDELMANN' AND GORDON EDLIN Department of Genetics, University of California, Davis, California 95616 Received for publication 21 March 1974

MATLAB file provided upon request.