Engineering strategy of yeast metabolism for higher alcohol production
© Matsuda et al; licensee BioMed Central Ltd. 2011
Received: 25 June 2011
Accepted: 8 September 2011
Published: 8 September 2011
While Saccharomyces cerevisiae is a promising host for cost-effective biorefinary processes due to its tolerance to various stresses during fermentation, the metabolically engineered S. cerevisiae strains exhibited rather limited production of higher alcohols than that of Escherichia coli. Since the structure of the central metabolism of S. cerevisiae is distinct from that of E. coli, there might be a problem in the structure of the central metabolism of S. cerevisiae. In this study, the potential production of higher alcohols by S. cerevisiae is compared to that of E. coli by employing metabolic simulation techniques. Based on the simulation results, novel metabolic engineering strategies for improving higher alcohol production by S. cerevisiae were investigated by in silico modifications of the metabolic models of S. cerevisiae.
The metabolic simulations confirmed that the high production of butanols and propanols by the metabolically engineered E. coli strains is derived from the flexible behavior of their central metabolism. Reducing this flexibility by gene deletion is an effective strategy to restrict the metabolic states for producing target alcohols. In contrast, the lower yield using S. cerevisiae originates from the structurally limited flexibility of its central metabolism in which gene deletions severely reduced cell growth.
The metabolic simulation demonstrated that the poor productivity of S. cerevisiae was improved by the introduction of E. coli genes to compensate the structural difference. This suggested that gene supplementation is a promising strategy for the metabolic engineering of S. cerevisiae to produce higher alcohols which should be the next challenge for the synthetic bioengineering of S. cerevisiae for the efficient production of higher alcohols.
The bioproduction of higher alcohols with more than 3 carbon atoms is desirable because they have the preferred properties of renewable liquid fuels and wide applications in commodity chemicals. In designing fermentation processes for mass production, the development of recombinant microbial strains is a critical first step . The pioneering achievements were demonstrated by the construction of metabolically engineered Escherichia coli strains that produce butanols and propanols. Due to insufficient genetic tools for the natural 1-butanol producer clostridia , E. coli has been engineered for 1-butanol fermentation by introducing the CoA-dependent clostridial pathway [3–7]. The production of 1-butanol was preliminary achieved in the range of 0.55 to 1.2 g/L [4, 6, 8]. The maximum 1-butanol titer (30 g/L) was achieved by the introduction of irreversible transenoyl-CoA reductase and the creation of NADH and acetyl-CoA driving forces [9, 10]. The production of higher alcohols, including 1-propanol, 1-butanol, isobutanol, 2-methyl-1-butanol, and 3-methyl-1-butanol, was also demonstrated by introducing the keto-acid pathway [8, 11–22]. This implementation resulted in 1-butanol production of approximately 0.85 g/L . In these studies, the production of the target alcohols was achieved by the introduction of the foreign genes required for their biosyntheses and by gene deletions to modulate the entire metabolism of the strains.
In this study, the potential production of higher alcohols by S. cerevisiae is compared to that of E. coli by employing in silico metabolic simulation techniques based on flux balance analysis (FBA). FBA is a mathematical approach for analyzing the flow of metabolites through a metabolic network [30–32]. The distribution of metabolic fluxes in the metabolic networks can be analyzed using the stoichiometric model of the metabolic reactions without knowledge of the metabolite concentrations or details of the enzyme kinetics [33, 34]. Although FBA assumes the ideal metabolism conditions by ignoring all dynamic aspects of metabolic regulations such as gene expression, feedback regulation, and posttranslational modifications, it has been demonstrated that FBA can evaluate the performance of a metabolic network [30, 33]. In this report, FBA-based metabolic simulation was demonstrated by following the strategy applied for the actual metabolic engineering. After reactions required for the biosynthesis of higher alcohols were introduced into the metabolic models, FBA-based metabolic simulations were performed for multiple gene-deletion mutants to evaluate the capabilities of the engineered strains to produce higher alcohols. For this purpose, the backbone metabolic models, which describe the essential structures of their central metabolism (Figure 1), were employed to reduce the number of gene-deletion combinations to be tested. By using the small backbone models, the performance of all single, double, triple, and quadruple deletion mutants could be comprehensively investigated within a realistic period. The in silico analysis was applied for the backbone models of both E. coli and S. cerevisiae to highlight differences between their metabolic networks. The comparative analyses revealed that the central metabolism of S. cerevisiae has limited potential for the efficient production of higher alcohols in comparison with that of E. coli. It is also predicted that its poor productivity can be improved by extension of the central metabolic network.
Construction of backbone models
The backbone metabolic models of E. coli and S. cerevisiae were employed for this analysis. The backbone metabolic models, which describe the essential structures of the central metabolism, were constructed from information from both the literature [35–41] and databases [42–44] (Figure 1 and Additional file 1). The backbone models for E. coli and S. cerevisiae are hereafter designated as iBKEco52 (i.e., an iB ioK E. co li metabolic model containing 52 reactions) and iBKSce50, respectively. In iBKSce50, the metabolic network is compartmentalized in the cytosol and mitochondria. Although the backbone models contain only 50 or 52 reactions, their behavior was similar to that of genome-scale models of E. coli (iJR904) and S. cerevisiae (iMM904)[45, 46] (Additional file 2). These original models were modified by the addition of reactions for the synthesis of each higher alcohol. As shown in Figure 1, the following 6 pathways were tested: (1) 1-propanol by oxaloacetate (OAA), (2) 1-butanol by AcCoA, (3) 1-butanol by OAA, (4) isobutanol by pyruvate (PYR), (5) 3-methylbutanol by PYR, and (6) isopentenol from AcCoA (Additional file 3). By using these models, the potential production capabilities of higher alcohols were compared between E. coli and S. cerevisiae.
Metabolic simulation of reaction-deleted mutants of E. coli
As the first step of the analysis, the metabolic performance of E. coli was evaluated as a reference for the comparison. The potential productions of higher alcohols by E. coli were determined by employing the FBA-based metabolic simulations. In the procedure, the metabolic flux distribution was optimized to maximize the cell growth rate . It is based on the assumption that a microbial metabolic system should evolve towards faster cell growth . As this assumption has been experimentally supported , it is expected that the product yield will be improved when the production of higher alcohols contributes to faster cell growth. Here, the FBA-based metabolic simulations were performed by maximizing metabolic flux for biomass production from glucose using the linear optimization method. The results revealed that no higher alcohols were produced from glucose in the all modified backbone models of E. coli. The low productivity demonstrated by the in silico metabolic models mirrors the poor performance of actual recombinant E. coli strains just after the introduction of genes required for higher alcohol biosynthesis [4, 8, 29].
To improve the yield of the target alcohols, the deletion of metabolism-related genes has been demonstrated to regulate the flux balances in the metabolic network [8, 11]. The genes, however, must be deleted with regard to both the product yield and cell growth because gene deletion often seriously hampers cell growth. Because the effects of gene deletions could not be predicted empirically, FBA-based metabolic simulations were performed to elucidate the optimal combination of genes to be deleted [49–52].
Via this methodology, the production of higher alcohols by E. coli was investigated by performing FBA-based metabolic simulations for all single, double, triple, and quadruple deletion mutants generated from the metabolic model (see Methods for the detailed procedure). In the analysis, reactions instead of genes were removed from the metabolic models. The simulation results were verified by comparisons with literature data. The metabolic engineering of E. coli demonstrated that the product yield of a recombinant E. coli strain expressing genes for 1-butanol or isobutanol biosynthesis was enhanced by deletions of genes such as ΔadhE, ΔldhA, ΔfrdBC, and Δpta as well as ΔadhE, ΔldhA, ΔfrdBC, and Δpfl, respectively [4, 8]. The results were reproduced by FBA-based metabolic simulations using the modified backbone models. The 1-butanol and isobutanol yields were increased to 0.14 and 0.19 (YCmol/Cmol glucose), respectively, by the deletions of the corresponding reactions.
The numbers of proper strains among all single, double, triple, and quadruple deletion mutants generated from the backbone models for E. coli (iBKEco52) and S. cerevisiae (iBKSce50, iBKSce50Δmit, and iBKSce50+7)
Target higher alcohols
Number of proper strains
Total (single/double/triple/quadruple deletion mutants)
1-propanol from OAA
1-Butanol from AcCoA
1-Butanol from OAA
Isobutanol from PYR
3-Methyl-1-butanol from PYR
Isopentenol from AcCoA
Metabolic simulation of reaction-deleted mutants of S. cerevisiae
In order to evaluate a performance of the in silico analysis using the backbone model of S. cerevisiae, iBKSce50, predicted growth rates of all single-reaction-deleted mutants were compared with the experimental data. The published phenotype data demonstrated that an inviable phenotype was observed for single gene-deleted mutants including Δpgi1, Δfba1, Δtpi1, Δpgk1, Δpyk1, and Δrki1 among the genes included in iBKSce50 [53–55]. Most results could be reproduced by the FBA-based metabolic simulation using iBKSce50 (Additional file 6). By using the backbone model of S. cerevisiae, iBKSce50, the potential metabolic performance of S. cerevisiae was also evaluated using the same procedure for E. coli, and the results were compared with that of E. coli. The FBA-based metabolic simulations for all single, double, triple, and quadruple deletion mutants indicated that the number of proper strains was smaller than that for E. coli for all target alcohols (Table 1). In particular, for the case of acetyl-CoA-derived higher alcohols, no or very few target-producing strains were observed (Figure 2a and Table 1). Exceptionally good results were observed for isobutanol, probably because the redox balance required for isobutanol biosynthesis is similar to that for ethanol (Figure 2c). In the case of the other pathways, such as that towards 1-propanol, actively growing and target-producing strains were not observed among the proper strains (Figure 2e). It was also demonstrated few genes could be deleted without decreasing cell growth (Figure 3d-e). These results suggest that the strategy employed for the engineering of E. coli metabolism should not be effective for a construction of S. cerevisiae over-producing higher alcohols.
Properties of the metabolic network
The network properties of the backbone models for E. coli (iBKEco52) and S. cerevisiae (iBKSce50, iBKSce50Δmit, and iBKSce50+7)
Number of nodes
Characteristic path length
Number of elementary modes
As the difference should be derived from the nature of the metabolic networks, 2 structural properties--network density and characteristic path length--were compared between the E. coli and S. cerevisiae backbone models [56, 57]. Here, a substrate-product pair was considered a pair of nodes connected by an undirected edge. The network density represents the density of reactions among metabolites, and it should be 1 when all metabolites are connected with each other. The observed network densities of the E. coli and S. cerevisiae backbone models were 0.117 and 0.092, respectively, indicating that the metabolites in the E. coli network are more densely connected by the metabolic reactions (Table 2). The characteristic path length indicates the average distances of all of the metabolite-metabolite pairs. For example, the distance between glucose and glucose-6-phosphate is 1 because they are directly connected by the reaction catalyzed by hexokinase. The determined characteristic path lengths suggest that the metabolites in E. coli are more closely connected, as the characteristic path length of E. coli is smaller than that of S. cerevisiae (Table 2). Although a relationship between those properties and higher alcohol production is unclear, the results suggest that the smaller number of elementary modes of S. cerevisiae backbone model is, at least in part, derived from the lesser network density and longer characteristic path length of the metabolic network.
Improvement of the higher alcohol productivity of S. cerevisiae by the addition of E. coli genes
To increase the network density and reduce the characteristic path length of the central metabolic network of S. cerevisiae, the metabolic structure was modified by considering 2 structural features. Because the metabolic networks of S. cerevisiae are compartmentalized into the cytosol and mitochondria, translocations of NADP+, NADPH, and acetyl-CoA between these compartments were prohibited in the backbone model (Figure 1). Here, a hypothetical metabolic network of S. cerevisiae was constructed by merging the cytosolic and mitochondrial networks and was designated iBKSce50Δmit. The network density and characteristic path length of iBKSce50Δmit were improved to 0.113 and 2.664, respectively, by which the number of elementary modes was also increased to 5,859 (Table 2). Another structural difference between E. coli and S. cerevisiae is the occurrence of various shortcuts in E. coli such as pyridine nucleotide transhydrogenase, the anaplerotic pathways, the Entner-Doudoroff pathway, and acetyl-CoA synthesis by pyruvate formate-lyase. To supplement these metabolic functions in S. cerevisiae, the 7 E. coli reactions encoded by pntAB, edd, pfl, pps, maeD, ppc, and mdh were added to the backbone metabolic model of S. cerevisiae as cytosolic reactions. The expanded model was designated as iBKSce50+7. Other reactions, such as those related to the TCA cycle and those catalyzed by large protein complexes, were arbitrarily removed from the inserted reactions. The expanded model exhibited improved network properties and a larger number of elementary modes (Table 2).
The comparative in silico analyses performed in this study indicated that E. coli and S. cerevisiae have distinct potentials for higher alcohol production that originate from structural differences in their central metabolic networks (Figure 1). As demonstrated by the FBA-based metabolic analyses, the behavior of the central metabolism of E. coli appears more flexible than that of S. cerevisiae. Here, the flexibility of the metabolic network indicates the variety of flux distributions taken by the metabolic network. Thus, after the introduction of the genes required for the biosynthesis of higher alcohols, productivity could be improved by gene deletions that restrict the range of flux distributions to produce the target alcohols (Figure 2). However, because the central metabolism in S. cerevisiae has limited flexibility, further gene deletions after the introduction of foreign genes usually results in a serious reduction in cell growth (Figure 2 and 3). These results suggest that the strategy employed for the metabolic engineering of E. coli would be ineffective for S. cerevisiae.
The FBA-based metabolic simulations performed in this study, however, ignored the detailed aspects of metabolic regulations [30, 47]. Because the kinetics of enzymatic reactions and the regulation of those activities were not considered, the results of the FBA-based analysis often over- or underestimated the role of metabolic pathways. This means that the FBA-based metabolic simulations could not predict the exact behavior of the metabolism of the microbe. To avoid these problems, metabolic performances derived from central metabolic networks were evaluated by employing the backbone metabolic models. Additionally, the production of higher alcohols in all single, double, triple, and quadruple deletion mutants were comprehensively determined to compare the overall trends of the metabolic performances of E. coli and S. cerevisiae. A possible drawback of the backbone model is the oversimplification of the metabolic network by omitting important metabolic functions. Although the details of yeast metabolism remain unclear, we reconstructed the backbone model by considering various studies and database informations [35–44].
If the stylized analysis performed in this study bears any resemblance to the real metabolism of E. coli and S. cerevisiae, the implications of this study for metabolic engineering of S. cerevisiae are radical. Due to its limited flexibility, the central metabolism of S. cerevisiae could not reach the flux distributions required for the effective production of higher alcohols. The comparison of the properties of metabolic network indicated that the cell compartmentalization and the lack of several shortcut reactions are possible causes of the low flexibility (Table 2). This implies that the functionality of the central metabolism of S. cerevisiae has to be supplemented by the addition of reactions (Table 2). Thus, the metabolic simulation demonstrated that the modified backbone model of S. cerevisiae possessing 7 E. coli reactions (iBKSce50+7) and the merged compartment (iBKSce50Δmit) had excellent production capabilities for the target alcohols (Figure 2b, d and 2f). Although the conclusion indicates a theoretical possibility for higher alcohol production, it is suggested that further modification of yeast metabolism requires the introduction of multiple genes and the coordinated regulation of their expression (Figure 4). Although the introduction of a single reaction to the central metabolism of S. cerevisiae has been attempted [58, 59], an innovative engineering methodology is required for implementing the strategy to the actual S. cerevisiae metabolism. This is the next challenge for the synthetic bioengineering of S. cerevisiae for the efficient production of higher alcohols.
The genome-scale models of E. coli (iJR904 GSM/GPR) and S. cerevisiae (iMM904) were downloaded from http://gcrg.ucsd.edu. The backbone models of E. coli (iBKEco52) and S. cerevisiae (iBKSce50) were reconstructed using the information from the literature [35–41] and the databases including EcoCyC (http://ecocyc.org/) and YEASTNET (http://www.comp-sys-bio.org/yeastnet/)[43, 44] (Supplementary Data S1). Elementary mode analysis was performed by the aid of METATOOL5.1 .
FBA-based metabolic simulation
The FBA-based metabolic simulation was performed via previously described methods  using MATLAB R2010b and glpk version 4.42 to perform the linear programming methods. The metabolic simulations were performed using the following procedure. (1) The linear programming was executed using the reactions for biomass production or growth rate as the objective function. The carbon source was fixed to be glucose consumed at 10 mmol gDW-1 h-1 in all analyses. (2) To avoid indefinite results, the flux for target production is minimized under the maximum growth rate condition. (3) The growth rates and target productivities were determined at 16 different oxygen uptake rates (0.1, 1, 2...,15 mmol). Those averages were considered the metabolic performance of the metabolic models. When the levels of growth speed were more than 1% of that of wild type, those deletion mutants were considered viable. The target-producing strains indicated the viable mutants producing target alcohols in yields exceeding YCmol/Cmol glucose = 0.01. Because most deletions in the target-producing strains are silent or have adverse effects, we defined "proper" strains as target-producing strains in which all deletions contributed to the improvement of product yield. The network density and the characteristic path length were determined with the aid of Network Analyzer version 2.7 .
This work was financed by Special Coordination Funds for Promoting Science and Technology, Creation of Innovation Centers for Advanced Interdisciplinary Research Areas (Innovative Bioproduction Kobe), MEXT, Japan.
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