Modelling Biochemical Reaction Networks Lecture 9: Glycerol - - PowerPoint PPT Presentation

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Modelling Biochemical Reaction Networks Lecture 9: Glycerol - - PowerPoint PPT Presentation

Modelling Biochemical Reaction Networks Lecture 9: Glycerol metabolism, Part I Marc R. Roussel Department of Chemistry and Biochemistry Glycerol metabolism Glycerol is one of the building blocks of lipids. Used as an energy source by


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SLIDE 1

Modelling Biochemical Reaction Networks Lecture 9: Glycerol metabolism, Part I

Marc R. Roussel Department of Chemistry and Biochemistry

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SLIDE 2

Glycerol metabolism

◮ Glycerol is one of the building blocks of lipids. ◮ Used as an energy source by conversion to a form that can be

injected into the glycolytic pathway:

4 2−

CH H

2 PO4 2−

CH

2 PO4 2−

CH

2 PO

HO H H CH2OH CH2OH C O CH OH

2

C

2O

OH O H C C C H HO C H

+

phosphate dihydroxyacetone

+

NADH + H glycerol glycerol 3−phosphate 3−phosphate

glycolysis

glyceraldehyde ADP kinase glycerol 3−phosphate dehydrogenase isomerase glycerol triose phosphate ATP NAD

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SLIDE 3

Flux through a pathway

◮ Rate at which material “moves through” a pathway ◮ To define a flux, need a “source” and a “sink” ◮ Options for a source: ◮ Constant glycerol ◮ Constant rate of addition of glycerol ◮ Options for a sink: ◮ Neglect reversibility of triose phosphate isomerase and make

D-glyceraldehyde 3-phosphate the sink

◮ Include one or more reactions from glycolysis, the last of which

is irreversible (in reality or by assumption)

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SLIDE 4

Questions

◮ Glycerol is a byproduct of various industrial processes

(production of soap, biodiesel, vegetable oil).

◮ We might want to use it as a feedstock for production of

(e.g.) yeast, for baking, brewing/fermenting, or sometimes used as nutritional supplements for cattle.

◮ What factor(s) limit the flux through this pathway? ◮ Can we engineer a strain of Saccharomyces cerevisiae that is

capable of a higher flux through this pathway?

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SLIDE 5

Glycolysis “payoff phase”

◮ We have to be careful not to “choke” glycolysis, so we should

model the relevant part of this pathway, the so-called “payoff phase”:

2

C H OH C O

2

C

2−

O

4 −

H PO

2− 4

PO C H C O

2

C O− H HO

2− 4

PO C H C O

2

C O− H OH C H O

4 − 4 2− 2 4 2−

C CH PO PO C CH PO C C O

3

C O− H O H OH C O

2

H kinase pyruvate phosphoenolpyruvate 2−phosphoglycerate kinase phosphoglycerate

+

NADH + H NAD+ 3−phosphate glyceraldehyde 3−phosphoglycerate enolase ADP ATP ATP ADP 1,3−bisphosphoglycerate pyruvate dehydrogenase glyceraldehyde 3−phosphate mutase phosphoglycerate

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SLIDE 6

Cosubstrates

◮ Several reactions have cosubstrates (ATP, ADP, NAD+, etc.). ◮ Treat as constant using typical in vivo values ◮ Resource: K. R. Albe et al., J. Theor. Biol. 143, 163 (1990). ◮ Must know rate law, which depends on order of binding and

  • ther details

◮ Issue can sometimes be ducked, depending on how parameters

were measured

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SLIDE 7

Locating enzyme parameters

◮ We need (a) rate law, (b) KM for each substrate, and (c) vmax

  • r (d) kcat and [E]total (vmax = kcat[E]total).

◮ Preferably need parameters for each enzyme from our target

  • rganism

◮ Useful resource: BRENDA, a database of enzyme kinetic

parameters (http://www.brenda-enzymes.org) Example: glycerol kinase

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Estimating the kinetic parameters of glycerol kinase in

  • S. cerevisiae

◮ KM(glycerol) = 2 mM [C. C. Aragon et al., J. Mol. Catal. B

52–53, 113 (2008)]

◮ BRENDA gives values of the turnover number (kcat) and of

the specific activity (vmax/cE, where cE is the concentration

  • f enzyme in g/L)

◮ Either way, need enzyme concentration to get vmax ◮ No values given for S. cerevisiae

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SLIDE 9

Estimating the kinetic parameters of glycerol kinase in

  • S. cerevisiae

◮ It would be unusual to measure a KM without also obtaining a

vmax, so go look at Aragon et al. (2008).

◮ vmax = 1.15 U/mL ◮ Methods, section 2.5: “One unit (U) of enzyme was defined as

the amount of the enzyme catalyzing the formation of 1 µmol

  • f glycerol-3-phosphate/min at 60◦C.”

◮ vmax = 1.15 µmol (mL)−1min−1 ≡ 19.2 µmol L−1s−1

Problem: Data given at 60◦C, not the 20–30◦C of industrial processes Rule of thumb: Rate constants approximately double for every 10◦C increase in temperature

◮ vmax at 20◦C should be about 24 times smaller than at 60◦C,

  • r about 1 µmol L−1s−1.
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SLIDE 10

Estimating the kinetic parameters of glycerol kinase in

  • S. cerevisiae

ATP as cosubstrate

◮ Issue not addressed by Aragon et al. (2008) ◮ Assays carried out in presence of a roughly physiological

concentration of ATP (2.6 mM, somewhat higher than the 1–2 mM usually found in yeast; Albe et al., 1990)

◮ Get effective rate law for that concentration of ATP ◮ Given uncertainties in other parameters, this should be OK.

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SLIDE 11

Estimating the kinetic parameters of glycerol kinase in

  • S. cerevisiae

Summary

vgk = vmax[glycerol] Kgk + [glycerol] with vmax = 1 µmol L−1s−1 Kgk = 2 mM

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SLIDE 12

Next time

◮ We could continue in this vein, and in some cases we have no

  • ther choice.

◮ Next time: another key resource that allows us to build on

  • ther people’s work