u.s. army combat capabilities development command … · i have addressed most of my research...
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UNCLASSIFIED//FOR OFFICIAL USE ONLY//DRAFT//PRE-DECISIONAL
UNCLASSIFIED//FOR OFFICIAL USE ONLY//DRAFT//PRE-DECISIONAL
U.S. ARMY COMBAT CAPABILITIES
DEVELOPMENT COMMAND –
ARMY RESEARCH LABORATORY
Leah A. Lewis, [email protected]
Hampton University
DoD HBCU/MI Summer Research Program
06 08 2020
Metabolic Modeling of Pseudomonas putida KT2440 to understand and improve the breakdown of plastic waste
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• PET plastics from water bottles, packaging: among
largest battlefield waste streams1
– Hard to recycle in remote areas
– Burn pits outlawed in Army2
– Biological process to break down PET attractive• Safe, mild conditions. Low energy input.
• Especially if it could generate useful chem, mat, energy
• PET comes from polymerization of terephthalic acid
(TPA) + ethylene glycol (EG)3
– Hydrolysis of PET returns to these monomers (toxic)
– P. putida: bacterium that can metabolize many org. compounds
– P. putida KT2440 (“KT”) can extract energy from EG
– Whether it can grow on EG as sole C-source unclear
– Most recent analyses indicate yes
BACKGROUND
PET water bottles 1
Army burn pit4
1. Conant, J. M. (2018, March 28). US Army lab finds plastic bottles, other waste products have re-use potential for battlefield. https://www.army.mil/article/202398/us_army_lab_finds_plastic_bottles_other_waste_products_have_re_use_potential_for_battlefield.
2. Preston, B. (2011, May 16). Attack of the Warzone Water Bottles. State of the Planet. https://blogs.ei.columbia.edu/2011/05/16/attack-of-the-warzone-water-bottles/.
3. Salvador, M. et al. (2019). Microbial Genes for a Circular and Sustainable Bio-PET Economy. Genes, 10(5), 373. https://doi.org/10.3390/genes10050373
4. Myers, M. (2019, July 12). Why DoD is still using burn pits, even while now acknowledging their danger. Military Times. https://www.militarytimes.com/news/your-military/2019/07/12/why-dod-is-still-using-burn-pits-even-while-now-acknowledging-their-danger/.
5. iGem. Degradation (2012). Team:TU Darmstadt. http://2012.igem.org/Team:TU_Darmstadt/Project/Degradation.
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We are interested in using whole-genome metabolic models of P. putida
to better-understand its potential to grow on and convert EG & TPA
• Do different methods of constructing and analyzing these models produce different
outputs?
– How do outputs compare to literature as models are updated over time?
• Can flux balance analysis (FBA) predict how well P. putida can grow on EG, TPA, or
both?
– What are the theoretical yields (limits) on what it can generate from a given set of
compounds in the growth medium?
• What do these models say about viability of a bioprocess based on P. putida to convert
EG & TPA into benign biomass or even useful chemicals?
• Can genetic modifications improve the ability of P. putida KT2440 to grow (produce
biomass) on EG and/or TPA as sole carbon sources?
RESEARCH QUESTIONS
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• Whole-Genome Metabolic Model: Reconstruction of all metabolic reactions an organism
can carry out & all compounds involved (“metabolic network”), based on contents of its
genome7
• Flux Balance Analysis (FBA): Calculation of “flow” of compounds through metabolic
network, given set of conditions & constraints. – Constraints represented by “objective functions,” e.g., “maximize biomass formation”8
– Strictly stoichiometric. No kinetics or thermodynamics involved.
• These modeling tools help us predict feasibility & limits of growth potential production
rate of important metabolites.
WHOLE-GENOME METABOLIC MODELS
AND FLUX BALANCE ANALYSIS
7. Nogales, et al. (2008). A genome-scale metabolic reconstruction of Pseudomonas putida KT2440: iJN746 as a cell factory. BMC Systems Biology, 2(1), 79. https://doi.org/10.1186/1752-0509-2-79
8. Orth, J. D., Thiele, I., & Palsson, B.Ø. (2010). What is flux balance analysis? Nature Biotechnology, 28(3), 245–248.
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v: (set of) possible flux vectors through all n reactions
S: stoichiometric matrix.
Sv = 0: conservation of mass
• Z: objective function to maximize
• Solution to this FBA is v that maximizes Z
Based on stoichiometry
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• Web-bases suite of “apps”
• US DOE Systems Biology Knowledgebase
• Metabolic model built for P. putida KT2440 with EG
as sole carbon source in the growth medium
• A flux balance analysis (FBA) was performed,
maximizing the biomass reaction flux
• Several reactions required for growth added
automatically by KBase
• “Gap filling” (not ideal)
• Results indicated biomass formation (growth) is
possible on EG by a plausible route
• Biomass flux of 0.10 h-1obtained on EG, vs.
0.46 h-1on glucose
FBA MODELING TOOL #1:
9. The U.S. Department of Energy Systems Biology Knowledgebase. KBase. http://kbase.us/.
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• COnstraint-Based Reconstruction and Analysis Toolbox for PYthon
• Requires a Python interpreter.
– Installed Anaconda3 Navigator freeware
– Learned required Python scripting with Software Carpentry (https://swcarpentry.github.io/python-novice-inflammation)
• Completed several COBRAPY lessons for building models, importing
growth media, and simulating FBA
• Reactions and metabolites comprising P. putida KT2440 models iJN746
(2008) & iJN1463 (2019) obtained from the BiGG Models database (http://bigg.ucsd.edu/search?query=pseudomonas+putida)
• COBRApy used to perform FBA on both models with EG as sole carbon
source
FBA MODELING TOOL #2:
10. GitHub. cobrapy - constraint-based metabolic modeling in Python. https://opencobra.github.io/cobrapy/.
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• KBase easy to use but slow. Many uploads/downloads, site closures for upgrades
– Models in KBase have little documentation or “quality ratings”
– Gapfilling algorithm not a good substitute for well-curated model
• COBRApy requires learning Python
– Higher-quality models, documented with publications, experimentally-validated
– Faster – Run FBAs without up/downloading each time
– Direct application of specific models: no gapfilling
• Tools not compatible with each other. Different data formats & notation
• Verdict: COBRApy requires more investment to learn, but worth it
KBASE VS. COBRAPY
11. KBase. https://narrative.kbase.us/#dataview/19217/162098/1.
12. The Regents of the University of California. (2019). BiGG Models. BiGG Model iJN1463. http://bigg.ucsd.edu/models/iJN1463.
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• Semi-Automated Metabolic Map Illustrator in
Python (SAMMIpy)13 used to render
COBRApy FBA results into metabolic
pathway diagrams
• SAMMIpy visualizations can be filtered to
show only the compounds and reactions
involved in the metabolism of EG.
• SAMMIpy diagrams useful to visualize
connections between enzymes ( ) &
metabolites ( )
• Upgrades would make tool more useful• Show fluxes on standard metabolic maps (e.g.
TCA cycle)
• More info, display options, & clearer
appearance for figures & presentations
VISUALIZATION OF FBA RESULTS
13. The University of Texas - MD Anderson Cancer Center. Semi-Automated Metabolic Map Illustrator. SAMMI. https://bioinformatics.mdanderson.org/public-software/sammi/.
Visualization of EG catabolism pathway &
fluxes by P. putida KT2440 model iJN1463
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• The BiGG database of metabolic models has 2 entries for P. putida KT2440,
both from the Palsson group at UCSD: – Model iJN746 from 200814 (“746”)
– Model iJN1463 from 201915 (“1463”)
• Model iJN1463 is the newest and most detailed model for P. putida KT2440,
which is can only analyzed through COBRApy.
• iJN1463 has enhancements over earlier models of KT244014,15:– Greater # of C- and N-sources
– More accurate prediction of growth capabilities, growth rates, flux distributions
– More detailed and accurate chemical formula for P. putida biomass
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14. Nogales, et al. (2008). A genome-scale metabolic reconstruction of Pseudomonas putida KT2440: iJN746 as a cell factory. BMC Systems Biology, 2(1), 79. https://doi.org/10.1186/1752-0509-2-79
15. Nogales, J., Mueller, J., Gudmundsson, S., Canalejo, F. J., Duque, E., Monk, J., Palsson, B.Ø. (2019). High‐quality genome‐scale metabolic modelling of Pseudomonas putida highlights its broad metabolic capabilities. Environmental Microbiology, 22(1), 255–269.
https://doi.org/10.1111/1462-2920.14843
A TALE OF TWO MODELS
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P. putida KT2440 model iJN1463 was able to grow (produce biomass) on ethylene
glycol, while model iJN746 could not
A TALE OF TWO MODELS (con’t)
• Biomass flux of 0.27 h-1 for iJN1463 on EG compares
favorably to 0.53 h-1 on glucose benchmark
• Analysis of EG (glycol) reaction steps reveal periplasm
active (ATP-consuming) glycolaldehyde (Gcald) transport
step
• Possible genetic engineering opportunity
• Functional expression of a passive transport channel
for EG or Gcald into cytoplasm
• Model predicts this would increase biomass flux to
0.41.
EG
Pa
ssiv
e im
port
Glycol
DHase
Gcald
AB
C tra
nsp
orte
r
ATP
ADP
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EG REACTIONS & FLUXES WITH iJN1463
Biomass flux: 0.269 h-1
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MODELING THE TPA METABOLISM SIDE OF PET
16. The International Genetically Engineered Machine Competition. pNB-Est 13: Esterase PET cleaving enzyme. Registry of Standard Biological Parts. http://parts.igem.org/Part:BBa_K808026.
17. (Pathway Diagram): The International Genetically Engineered Machine Competition. PlastiCure. iGEM. http://2015.igem.org/Team:Pasteur_Paris/Description
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• Neither iJN1463 nor the entire BiGG
database has an entry for TPA!
• Plenty of literature on TPA metabolism
in other microbes, e.g. Rhodococcus3
• The first TPA breakdown product in
iJN1463 is protocatechuate (PCA)
• I have started modeling PCA
metabolism by iJN1463
• If P. putida cannot convert TPA to PCA
another opportunity for genetic
engineering (add genes for enzymes)
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PCA REACTIONS & FLUXES WITH iJN1463
Biomass flux: 0.289 h-1
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iJN1463 WITH EG AND PCA (DUAL C-SOURCES)
P. putida KT2440 model iJN1463 with EG and
PCA as dual C-sources• Same biomass flux of 0.289 as above with PCA
alone!
• Co-utilization not predicted by model to maximize
growth
• Looks like “Diauxic” metabolism
– Commonly seen with sugars, e.g. glucose & lactose
– Controlled by complex genetic regulatory switches
– But, regulation not part of metabolic models
(stoichiometry only)
• Model predicts P. putida will exhaust all PCA
before transitioning to EG
– Only because 0.289 > 0.269 (or weighted average)
& model told to maximize biomass flux
– “Synergy” required to have model use both (e.g.
redox balanced only with both substrates)
• Should be skeptical & test by experiment
0.289 h-10.269 h-1
Together: 0.289 h-1
(only PCA metabolized)
(PCA)
(EG)
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I evaluated 2 major genome-scale metabolic modeling platforms:• KBase, COBRApy
• Learned Python scripting language to run COBRApy
• Recommend COBRApy for quality of models.
• Unfortunately, the tools utilize incompatible data formats
I have addressed most of my research questions:• Different FBA tools & models can produce different answers
– Highest quality & most recent model for P. putida is iJN1463, not on KBase
• Analysis of iJN1463 indicates growth potential of P. putida on EG – About half of potential biomass flux on glucose: 0.27 vs. 0.53 h-1
– Possible improvement to 0.41 h-1 by engineering passive transport into cytoplasm
• Have begun to model TPA metabolism by P. putida– TPA not in BiGG, premier database of metabolic models
– Started with FBA models from PCA (2 steps down) similar biomass flux to EG
– FBA models with EG and PCA as dual C-sources predict PCA used first, not simultaneous consumption
• Additional investigation required about TPAPCA enzymes & transporters in P. putida– Literature, BLAST searches, or experiments in lab
– TPAPCA steps known in other bacteria, could be engineered into P. putida
• Results on PCA + EG allow evaluation of P. putida for both PET monomers– Diauxic consumption of PCA first, then EG not ideal for process
– Model’s prediction should be tested experimentally
– If verified, strategy to consume EG & TPA together: mixed consortium of P. putida + an EG consumer
– EG consumer could be P. putida with knockout of early TPA pathway step(s)
SUMMARY AND NEXT STEPS
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ACKNOWLEDGMENTS
Dr. Alex Tobias Dr. Matthew Perisin