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Background: The branched chain alcohol isobutanol exhibits superior physicochemical properties as an alternative biofuel. The yeast Saccharomyces cerevisiae naturally produces low amounts of isobutanol as a by-product during fermentations, resulting from the catabolism of valine. As S. cerevisiae is widely used in industrial applications and can easily be modified by genetic engineering, this microorganism is a promising host for the fermentative production of higher amounts of isobutanol.
Results: Isobutanol production could be improved by re-locating the valine biosynthesis enzymes Ilv2, Ilv5 and Ilv3 from the mitochondrial matrix into the cytosol. To prevent the import of the three enzymes into yeast mitochondria, N-terminally shortened Ilv2, Ilv5 and Ilv3 versions were constructed lacking their mitochondrial targeting sequences. SDS-PAGE and immunofluorescence analyses confirmed expression and re-localization of the truncated enzymes. Growth tests or enzyme assays confirmed enzymatic activities. Isobutanol production was only increased in the absence of valine and the simultaneous blockage of the mitochondrial valine synthesis pathway. Isobutanol production could be even more enhanced after adapting the codon usage of the truncated valine biosynthesis genes to the codon usage of highly expressed glycolytic genes. Finally, a suitable ketoisovalerate decarboxylase, Aro10, and alcohol dehydrogenase, Adh2, were selected and overexpressed. The highest isobutanol titer was 0.63 g/L at a yield of nearly 15 mg per g glucose.
Conclusion: A cytosolic isobutanol production pathway was successfully established in yeast by re-localization and optimization of mitochondrial valine synthesis enzymes together with overexpression of Aro10 decarboxylase and Adh2 alcohol dehydrogenase. Driving forces were generated by blocking competition with the mitochondrial valine pathway and by omitting valine from the fermentation medium. Additional deletion of pyruvate decarboxylase genes and engineering of co-factor imbalances should lead to even higher isobutanol production.
Stereoisomere Aromastoffe XIX: Asymmetrische Reduktion von 4(5)-Oxocarbonsäuren mit Bäckerhefe
(1987)
Asymmetric reduction of 4(5)-oxocarboxylic acids (esters)by baker’s yeast and cyclizationin acidic media yield soptically active γ(δ)lactones. The evaluation of their chirality and optical purity was carried out by HPLC (HRGC)analysis of the corresponding 1,4(1.5)-diols via diastereomeric esters with(R)-Mosher acid(MTPA) and (S)-O-acyllactic acids respectively. By increasing the 4(5)alkyl side chain 4R(5R) configurated γ(δ)-lactones with high ee-values are generated.
Background: The ideal biofuel should not only be a regenerative fuel from renewable feedstocks, but should also be compatible with the existing fuel distribution infrastructure and with normal car engines. As the so-called drop-in biofuel, the fatty alcohol 1-octanol has been described as a valuable substitute for diesel and jet fuels and has already been produced fermentatively from sugars in small amounts with engineered bacteria via reduction of thioesterase-mediated premature release of octanoic acid from fatty acid synthase or via a reversal of the β-oxidation pathway.
Results: The previously engineered short-chain acyl-CoA producing yeast Fas1R1834K/Fas2 fatty acid synthase variant was expressed together with carboxylic acid reductase from Mycobacterium marinum and phosphopantetheinyl transferase Sfp from Bacillus subtilis in a Saccharomyces cerevisiae Δfas1 Δfas2 Δfaa2 mutant strain. With the involvement of endogenous thioesterases, alcohol dehydrogenases, and aldehyde reductases, the synthesized octanoyl-CoA was converted to 1-octanol up to a titer of 26.0 mg L−1 in a 72-h fermentation. The additional accumulation of 90 mg L−1 octanoic acid in the medium indicated a bottleneck in 1-octanol production. When octanoic acid was supplied externally to the yeast cells, it could be efficiently converted to 1-octanol indicating that re-uptake of octanoic acid across the plasma membrane is not limiting. Additional overexpression of aldehyde reductase Ahr from Escherichia coli nearly completely prevented accumulation of octanoic acid and increased 1-octanol titers up to 49.5 mg L−1. However, in growth tests concentrations even lower than 50.0 mg L−1 turned out to be inhibitory to yeast growth. In situ extraction in a two-phase fermentation with dodecane as second phase did not improve growth, indicating that 1-octanol acts inhibitive before secretion. Furthermore, 1-octanol production was even reduced, which results from extraction of the intermediate octanoic acid to the organic phase, preventing its re-uptake.
Conclusions: By providing chain length control via an engineered octanoyl-CoA producing fatty acid synthase, we were able to specifically produce 1-octanol with S. cerevisiae. Before metabolic engineering can be used to further increase product titers and yields, strategies must be developed that cope with the toxic effects of 1-octanol on the yeast cells.
As fossil resources are diminishing, environmental concerns arise and chemical synthesis often involves expensive catalysts or extensive extraction procedures, the demand for production of industrially relevant compounds from renewable resources increases. In this context, engineering microorganisms for production of specialty chemicals, such as 3-alkylphenols, presents an attractive, environmental-friendly approach. 3-alkylphenols have various applications: due to their antiseptic and stabilizing properties many 3-alkylphenols, including 3-methylphenol (3-MP), are utilized as additives in disinfectant reagents and biological products, while they can be also implemented as platform chemicals for production of lubricating oil additives or flavors. Some 3-akylphenols have potential for transmission control of the disease sleeping sickness that is transmitted by tsetse flies in sub-saharan Africa, since 3-ethylphenol (3-EP) and 3-propylphenol (3-PP) and to a lesser degree 3-MP were found to attract tsetse flies and improved catch rates in impregnated tsetse fly traps. Microbial fermentation of 3-alkylphenols would provide a simple and inexpensive way for local communities in Africa to produce these compounds and prepare their own tsetse fly traps.
Some molds synthesize 3-MP as an intermediate during biosynthesis of the mycotoxin patulin. However, the heterologous host Saccharomyces cerevisiae has advantageous traits for industrial application, since it is well characterized, robust, simple to handle and easily genetically accessible. In this thesis, genetical engineering approaches were utilized to establish the yeast S. cerevisiae for biotechnological production of 3-alkylphenols. As a proof of concept, the iterative polyketide synthase from Penicillium patulum, 6-methylsalicylic acid synthase (MSAS), and 6-methylsalicylic acid (6-MSA) decarboxylase PatG from Aspergillus clavatus were heterologously expressed in S. cerevisiae resulting in the first reported de novo biosynthesis of 3-MP via 6-MSA in yeast from sugars (Hitschler & Boles, 2019). It was shown that codon-optimization and genomic integration of heterologous genes, high initial cell densities and a balanced expression of PatG were beneficial for heterologous production of up to 589 mg/L 3-MP in S. cerevisiae. However, toxicity of 3-MP limited higher product accumulation.
Different in vivo detoxification strategies were implemented to face this bottleneck. Growth tests revealed that 3-methylanisole (3-MA) is less toxic to the yeast cells than 3-MP. Expression of an orcinol-O-methyltransferase from chinese rose hybrids (OOMT2) was combined with in situ extraction converting the toxic 3-MP product into the volatile 3-MA and accumulating up to 211 mg/L 3-MA in the dodecane phase. Alternatively, up to 533 mg/L 3-MP glucoside were synthesized by expression of a UDP-glycosyltransferase (UGT72B27) from Vitis vinifera in the 3-MP producing strain, revealing saccharose as beneficial carbon source and ethanol growth phase as essential for high 3-MP production, although 3-MP conversions were not yet complete. Both detoxification strategies allowed circumvention of the toxicity imposed limited product accumulation. This was demonstrated when both detoxification strategies were combined with redirection of the carbon flux through deletion of phosphoglucose isomerase gene PGI1 and feeding a mixture of fructose and glucose leading to majorly improved product formation, with up to 899 mg/L 3-MA/3-MP and 873 mg/L 3-MP/3-MP glucoside, compared to less than 313 mg/L product titers in the wild type controls (Hitschler & Boles, 2020).
For provision of the tsetse fly attractants 3-EP from propionyl-CoA and 3-PP from butyryl-CoA, the substrate promiscuities of MSAS and PatG were exploited. However, slower formation rates with the alternative substrates propionyl-CoA and butyryl-CoA suggested that competing formation of 6-MSA from the preferred priming unit acetyl-CoA was dominating in vivo. Indeed, 3-EP or 3-PP formation was not observed in 3-MP producing yeast strains. Assuming that intracellular levels of propionyl-CoA and butyryl-CoA were limiting 3-EP and 3-PP formation, different strategies were implemented to raise the supply of these alternative priming units and successfully compete with acetyl-CoA for MSAS priming.
Supplementation of propionate increased propionyl-CoA levels by endogenous pathways sufficiently to enable 3-EP formation in yeast mediated by MSAS and PatG. Deletion of the 2-methylcitrate synthases CIT2 and CIT3 revealed that degradation of propionyl-CoA was not limiting 3-EP formation at this stage. In order to raise propionyl-CoA levels further, a heterologous propionyl-CoA synthase (PrpE) was expressed in the 3-MP producing yeast strain leading to up to 12.5 mg/L 3-EP with propionate feeding and blockage of degradation. Moreover, PrpE enabled also 3-EP formation without propionate supplementation suggesting that an endogenous supply of propionate existed that was reactivated by PrpE. As threonine or 2-ketobutyrate feeding increased 3-EP titers in combination with PrpE, this indicated that threonine degradation via 2-ketobutyrate was responsible for the endogenous propionate supply. Moreover, expression of branched-chain ketoacid dehydrogenase complex from Pseudomonas putida combined with PrpE provided propionyl-CoA from endogenous 2-ketobutyrate and raised 3-EP titers up to 5.9 mg/L compared to 2.8 mg/L with only PrpE indicating a potential route for optimization of 3-EP titers independent of propionate or threonine feeding.
For 3-PP production from butyryl-CoA, a heterologous ‘reverse ß-oxidation’ pathway was introduced in the 3-MP producing yeast strain providing sufficient butyryl-CoA for biosynthesis of up to 2 mg/L 3-PP. Degradation of the precursor via ß-oxidation was slightly limiting, since deletion of fatty acyl-CoA oxidase POX1 increased 3-PP titers slightly to 2.6 mg/L.
As the concentrations of 3-alkylphenols are close to the concentrations implemented in tsetse fly traps, the engineered yeast strains have the potential for simple and inexpensive on-site production of 3-alkylphenols as tsetse fly attractants by local rural communities in Africa. In spite of this success, 3-MP remained the main product in the developed yeast strains. Since 3-EP and 3-PP are more efficient tsetse fly attractants, a shift in substrate specificities of MSAS and PatG is desirable for a more favorable 3-EP/3-MP and 3-PP/3-MP product ratio regarding tsetse fly attraction. During rational engineering of MSAS, the MSASQ625A/I752V mutant showed a beneficial shift of product ratios with up to 11 mg/L 3-EP/63 mg/L 3-MP and 4.5 mg/L 3-PP/116 mg/L 3-MP, compared to a higher proportion of 3-MP with up to 343 mg/L, 11 mg/L 3-EP and 1.5 mg/L 3-PP in the wild type controls. Further engineering of MSAS and PatG might majorly improve production of 3-EP and 3-PP.
In summary, this thesis successfully established the yeast S. cerevisiae as cell factory for production of different 3-alkylphenols optimizing expression of the heterologous production pathway, elucidating means to detoxify products and establishing different approaches to increase intracellular levels of acyl-CoA precursors. The engineered yeast strains can be potentially implemented for simple and inexpensive fermentation of tsetse fly attractants in Africa.
Genetic engineering of baker’s and wine yeasts using formaldehyde hyperresistance-mediating plasmids
(1997)
Yeast multi-copy vectors carrying the for maldehyde-resistance marker gene SFA have proved to be a valuable tool for research on industrially used strains of Saccharomyces cerevisiae. The genetics of these strains is often poorly understood, and for various reasons it is not possible to simply subject these strains to protocols of genetic engineering that have been established for laboratory strains of S. cerevisiae. We tested our vectors and protocols using 10 randomly picked baker’s and wine yeasts all of which could be transformed by a simple protocol with vectors conferring hyperresistance to formaldehyde. The application of formaldehyde as a selecting agent also offers the advantage of its biodegradation to CO2 during fermentation, i.e., the selecting agent will be consumed and therefore its removal during down-stream processing is not necessary. Thus, this vector provides an expression system which is simple to apply and inexpensive to use. Key words: · Yeast · Transformation · Hyperresistance to formaldehyde