| Literature DB >> 28899034 |
Abstract
Over the last 15 years, several genome-scale metabolic models (GSMMs) were developed for different yeast species, aiding both the elucidation of new biological processes and the shift toward a bio-based economy, through the design of in silico inspired cell factories. Here, an historical perspective of the GSMMs built over time for several yeast species is presented and the main inheritance patterns among the metabolic reconstructions are highlighted. We additionally provide a critical perspective on the overall genome-scale modeling procedure, underlining incomplete model validation and evaluation approaches and the quest for the integration of regulatory and kinetic information into yeast GSMMs. A summary of experimentally validated model-based metabolic engineering applications of yeast species is further emphasized, while the main challenges and future perspectives for the field are finally addressed. © FEMS 2017.Entities:
Keywords: cell factory; constraint-based modeling; genome-scale metabolic model; metabolic engineering; metabolism; yeast
Mesh:
Year: 2017 PMID: 28899034 PMCID: PMC5812505 DOI: 10.1093/femsyr/fox050
Source DB: PubMed Journal: FEMS Yeast Res ISSN: 1567-1356 Impact factor: 2.796
Figure 1.Metabolic network reconstruction and mathematical modeling of genome-scale networks. (A) A draft metabolic network can be generated using genomic, biochemical and physiological information available in primary literature or proper databases. All annotated metabolic genes are first matched to enzymes and then to the reactions—composed by different metabolites and cofactors—to obtain GPR associations. Reactions are assembled into pathways which together constitute the metabolite network. Localization has also to be considered since chemically identical metabolites may be present in different cellular compartments. (B) The reconstructed genome-scale metabolic network is then transformed into a constraint-based model, by first converting it to a mathematical representation using a stoichiometric matrix (S) of the metabolite coefficients in each reaction, and further assuming pseudo-steady state and constraining the reaction flux (v) bounds. The system of linear equations defines the admissible flux space of solutions (known as flux cone) and using an objective function defining an optimization problem it is possible to find optimal solutions for a desired output. To simulate model growth and obtain meaningful flux distributions, information on biomass composition and ATP requirements of the cell must also be available. The generation of high-end genome-scale metabolic models often requires several cycles of testing and refinement based on the comparative results of in silico simulations and experimental data.
Figure 2.Evolutionary timeline of yeast GSMMs and their reconstruction inheritances. Each box contains the name of the metabolic model and is colored according to the respective yeast species color caption. Several GSMMs were reconstructed using previously available large-scale models as templates, from the same or different yeast species, which is represented in the figure through bold arrows connecting the respective boxes. The light-dashed colored lines represent the networks’ relationship regarding the models that, although did not serve as structural scaffolds, have been used in the comparative/validation process of the subsequent GSMM.
Figure 3.Genome-scale models of yeast in numbers. (A) Number of published GSMMs of yeast species over time. (B) Number of total genes, reactions (drains excluded), internal metabolites, intracellular compartments and reactions associated with genes of each GSMM. Inside each species categorization and if there is more than one GSMM for the same yeast, models are organized by date of publication (from top to down).
A selection of experimentally validated model-based metabolic engineering applications/studies of different yeast species.
| Organism | Target product | Model/method | Results | Reference (year) |
|---|---|---|---|---|
|
| Bioethanol | iFF708/FBA | 40% reduced glycerol yield on glucose and increased ethanol yield (+3%) without affecting the maximum specific growth rate | Bro |
|
| Sesquiterpenes | iFF708/OptGene | 85% increase in the final cubebol titer | Asadollahi |
|
| Vanillin | iFF708/OptGene | 1.5-Fold higher vanillin β-D-glucoside yield in batch mode, 2-fold productivity improvement in continuous culture | Brochado |
|
| 2,3-Butanediol | iMM904/Optknock | 2,3-Butanediol titer: 2.29 g l−1; Product yield: 0.113 g.g−1 under anaerobic conditions | Ng |
|
| Fumaric acid | iND750/literature mining + FBA | Titer: ∼1.68 g l–1 in batch culture | Xu |
|
| Malate | iNX804/FBA | Malate titer: 8.5 g l−1 | Chen |
|
| Succinate | iFF708/OptGene | 30- and 43-fold improvements in succinate titer and succinate yield on biomass, respectively | Otero |
|
| Amorphadiene | iMM904/FDCA | 8- to 10-fold greater product yield compared to the wild type | Sun |
|
| Acetoin | iNX804/FBA | Final acetoin titer: 3.67 g l−1 | Li |
|
| Human recombinant protein | PpaMBEL1254/MOMA and FSEOF | Enhanced recombinant protein yield up to 40% | Nocon |
|
| Fumaric acid | iNX804/NS | Final fumarate titer: 8.83 g l−1 | Chen |
|
| Lipids | iMK735/dFBA | Byproduct (citrate) formation was reduced and lipid production yield increased | Kavšček |
|
| 3HP | iTO977/pFBA | 3HP titer: 9.8 g l−1; Yield: 13 % C-mol C-mol−1 glucose | Kildegaard |
|
| β-Farnesene | iLL672 (extended version)/pFBA | Farnese yield: 17.3% g g−1 Productivity: 2.24 g l−1 h−1 (requiring 75% less oxygen) | Meadows |
FDCA—flux distribution comparison analysis.
NS—Not specified.
Dynamic FBA.
Parsimonious enzyme usage FBA.