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Case Study 3

Engineering an E. coli metabolic network for carbon fixation

Step 1: Model selection

The genome-scale metabolic model iJO1366 of E. coli was selected for this study. The model in .mat format was downloaded from the BiGG database and uploaded through Upload Options in NAViFluX. Growth conditions were defined using M9 minimal medium, consistent with the original study. Environmental uptake constraints were applied using NAViFluX, following the procedure in Case Study 1.

Model selection

Step 2: Constructing the engineered mutant model A “mutant” metabolic network was created by simulating gene deletions and enzyme insertions using NAViFluX. Following reactions were deleted from the model, using "Delete Reaction" option in NAViFluX.

Phosphoglycerate mutase (PGM), Glucose-6-phosphate dehydrogenase (G6PDH2r),Phosphofructokinase (PFK),Glyoxylate shunt reactions (ICL, MALS, ICDHx)

PGM

G6PDH2r

PFK

Step 3: Addition of Calvin–Benson–Bassham (CBB) cycle enzymes

The CBB cycle enzymes RuBisCO (RBPC) and phosphoribulokinase (PRUK) were added to the model using "Select Metabolite for New Reaction option". For adding PRUK reaction "ru5p__D_c" metabolite form Pentose Phosphate Pathaway was clicked, and to add RBPC "rb15bp_c" metabolite was clicked.

PRUK

PRUK

RBPC

RBPC

After adding PRUK and RBPC

Step 4: The updated model was downloaded with "Download Options" in .mat format and used for further analyses.

Download model

Step 5: Defining pyruvate uptake constraints.

The updated model was uploaded again to the NAVIFluX and Pyruvate uptake (Lower bound of "Ex_Pyr_e"") was constrained to 16 mmol/(gDW·hr), as reported experimentally.

Pyruvate uptake

Step 6: Cycle-free flux balance analysis

After defining the Pyruvate uptake Cycle Free Flux (cFBA) was choosen, with "BIOMASS_Ec_iJO1366_WT_53p95M" as Cellular objective.

cFBA

A growth rate of 23 mmol/(gDW·hr) was predicted, consistent with published experimental and modeling studies.

Step 7: Optimizing pyruvate uptake

Pyruvate uptake was systematically reduced to study its impact on acetate and CO₂ release. Each time "Ex_pyr_c" lower bound was set to -16.7, -13.36, -10.02, -6.68, -3.34 and 0. cFBA was performed each time, flux profiles were downloaded. The reaction fluxes of "BIOMASS_Ec_iJO1366_WT_53p95M", "Ex_ac_e", "Ex_Co2_e" fluxes were noted each time.

Optimization

Step 8: Exploring alternative carbon sources.

After determining that "Ex_ac_e" was 0 when "Ex_pyr_e" was -3.34, alternative Carbon sources were also tested. For instance Ex_Glyc_e lower bound was set to -1000, with Ex_pyr_e at 0, It's observed that Ex_Glyc_e flux was -6.51, and "BIOMASS_Ec_iJO1366_WT_53p95M", Ex_ac_e, Ex_co2_e were noted down.

Ex_Glyc_e

Similarly Ex_xyl__D_e lower bound also set to -1000, and the corresponding reaction fluxes were noted down.

Ex_xyl__D_e

Step 9: Finalising the Carbon uptake.

After multiple comparisons, Ex_pyr_e at lower bound -4 and Ex_Glyc_e at lower bound -7, was finalised at which "BIOMASS_Ec_iJO1366_WT_53p95M" is maximum and Ex_Co2_e and Ex_ac_e were minimum.