David Reckhow CEE 370 L#13 1
CEE 370 Environmental Engineering Principles
Lecture #13 Environmental Biology II
Metabolism Reading: Mihelcic & Zimmerman, Chapter 5
Davis & Masten, Chapter 3
Updated: 16 October 2019
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CEE 370 Environmental Engineering Principles Lecture #13 - - PowerPoint PPT Presentation
Print version Updated: 16 October 2019 CEE 370 Environmental Engineering Principles Lecture #13 Environmental Biology II Metabolism Reading: Mihelcic & Zimmerman, Chapter 5 Davis & Masten, Chapter 3 David Reckhow CEE 370 L#13 1
David Reckhow CEE 370 L#13 1
Metabolism Reading: Mihelcic & Zimmerman, Chapter 5
Davis & Masten, Chapter 3
Updated: 16 October 2019
Print version
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Types of Microorganisms
Bacteria Viruses Protozoa Rotifers Fungi
Metabolism Microbial Disease Microbial Growth
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Metabolites (wastes)
Biosynthesis (Anabolism) Energy Production (Catabolism)
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From: Sawyer, McCarty & Parkin, 1994; also: Sawyer & McCarty, 1978
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7.3 kcal per mole
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2 ATP 2 ADP 4 ADP 4 ATP 2 NAD+ 2 NADH
Net result: 2 ATPs
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If we have aerobic metabolism, rather than fermentation, energy from NADH may be harvested.
NADH + H + 3 PO + 3ADP + O NAD+ + 3ATP + H O
+ 4 3- 2 2 12
→
This gives us 6 more ATPs. Then the pyruvate may be further
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Generalized
Also showing
ATP NAD
From: Sawyer, McCarty & Parkin, 1994; also: Sawyer & McCarty, 1978
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Storage of Energy
Photosynthesis
Release of Energy
Respiration
Energy transfers by organisms are
5-50% capture
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A Redox reaction
Oxidation of Carbon Reduction of oxygen or some other
− + +
+ → + e H CO O H O H C 4 4 ) (
2 2 2
O H e H O
2 2
2 4 4 → + +
− +
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Nitrate Manganese Iron Sulfate Fermentation
2 3 2 2 3 2 )
− −
2 2 2 4 2 )
+ +
2 2 2 3 2 )
+ +
2 2 2 2 4 2 )
− 2 4 2 )
Ecological Redox Sequence
methanogenesis
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Contribution to
Bottom waters of
(Effler, 1997) Aerobic 39% Nitrate Reduction 10% Sulfate Reduction 27% Iron Reduction 1% Methano- genesis 23%
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Principles of Gibbs
From: Sawyer, McCarty & Parkin, 1994; also: Sawyer & McCarty, 1978
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Energy Balance
Cell synthesis (Rc) Energy (Ra) Electron acceptor
From: Sawyer, McCarty & Parkin, 1994; also: Sawyer & McCarty, 1978
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Portions of electron
Synthesis (fs) Energy (fe)
Values are for
From: Sawyer, McCarty & Parkin, 1994; also: Sawyer & McCarty, 1978
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Oxidation
Toluene dioxygenase (TDO)
From: Sawyer, McCarty & Parkin, 1994; also: Sawyer & McCarty, 1978
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Photoheterotrophs (rare) Photoautotrophs (primary producers) Chemoheterotrophs (organotrophs) Chemoautotrophs (lithotrophs)
Nitrifying, hydrogen , iron and sulfur bacteria Most bacteria, fungi, protozoa & animals Cyanobacteria, algae & Plants Purple and green non- sulfur bacteria
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Highly dependent on:
Temperature pH
From: Sawyer, McCarty & Parkin, 1994; also: Sawyer & McCarty, 1978
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Many ways of illustrating the steps
Substrate(s) bond to active site Product(s) form via transition state Product(s) are released
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Irreversible
Single intermediate
The overall rate is determined by the RLS, k2 But we don’t know [ES], so we can get it by the SS mass
balance
Again, we only know [Eo] or [Etot], not free [E], so:
2 1 1
−
E + S ES → E + P
→ ←
k1 k-1 k2
] [ ] [ ] [
2 ES
k dt P d dt S d r = = − ≡
2 1 1
−
Note that some references use k2 for k-1, and k3 for k2
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components for simple single intermediate enzyme reaction
Shaded block shows steady
state intermediates
Assumes [S]>>[E]t From Segel, 1975; Enzyme
Kinetics
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And solving for [ES],
1 2 1 1
− 2 1 1 1
−
1 2 1
k k k
+
−
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Irreversible
Single intermediate
max 2
1 2 1
s k k k
+
−
E + S ES → E + P
→ ←
k1 k-1 k2
2 ES
1 2 1
] [ ] ][ [ ] [
k k k
S E ES
+
−
+ =
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Substrate Concentration
20 40 60 80 100 120
Reaction Rate
20 40 60 80 100
rmax
0.5rmax
Ks
Classical substrate plot
max
s +
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utilization rate, U
And the maximum rates are then
max
s +
Y YX dt dX X r U µ ≡ = ≡ Y k U
max max
µ ≡ ≡
s +
and
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Lineweaver-Burke
Double reciprocal plot
Wikipedia version Voet & Voet version
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