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Highlights
• Different NADPH supply strategies are compared in Saccharomyces cerevisiae.
• Example products are d-xylitol and l-galactonate.
• ZWF1 overexpression is the most robust strategy in the diauxic batch fermentation.
• Carbon source dependencies and interferences of different strategies are explored.
Abstract
Enhancing the supply of the redox cofactor NADPH in metabolically engineered cells is a critical target for optimizing the synthesis of many product classes, such as fatty acids or terpenoids. In S. cerevisiae, several successful approaches have been developed in different experimental contexts. However, their systematic comparison has not been reported. Here, we established the reduction of xylose to xylitol by an NADPH-dependent xylose reductase as a model reaction to compare the efficacy of different NADPH supply strategies in the course of a batch fermentation, in which glucose and ethanol are sequentially used as carbon sources and redox donors. We show that strains overexpressing the glucose-6-phosphate dehydrogenase Zwf1 perform best, producing up to 16.9 g L−1 xylitol from 20 g L−1 xylose in stirred tank bioreactors. The beneficial effect of increased Zwf1 activity is especially pronounced during the ethanol consumption phase. The same notion applies to the deletion of the aldehyde dehydrogenase ALD6 gene, albeit at a quantitatively lower level. Reduced expression of the phosphoglucose isomerase Pgi1 and heterologous expression of the NADP+-dependent glyceraldehyde-3-phosphate dehydrogenase Gdp1 from Kluyveromyces lactis acted synergistically with ZWF1 overexpression in the presence of glucose, but had a detrimental effect after the diauxic shift. Expression of the mitochondrial NADH kinase Pos5 in the cytosol likewise improved the production of xylitol only on glucose, but not in combination with enhanced Zwf1 activity. To demonstrate the generalizability of our observations, we show that the most promising strategies – ZWF1 overexpression and deletion of ALD6 - also improve the production of l-galactonate from d-galacturonic acid. Therefore, we expect that these findings will provide valuable guidelines for engineering not only the production of xylitol but also of diverse other pathways that require NADPH.
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.
Pectin-rich residues are considered as promising feedstocks for sustainable production of platform chemicals. Enzymatic hydrolysis of extracted sugar beet press pulp (SBPP) releases the main constituent of pectin, d-galacturonic acid (d-GalA). Using engineered Saccharomyces cerevisiae, d-GalA is then reduced to l-galactonate (l-GalOA) with sorbitol as co-substrate. The current work addresses the combination of enzymatic hydrolysis of pectin in SBPP with a consecutive optimized biotransformation of the released d-GalA to l-GalOA in simple batch processes in stirred-tank bioreactors. Process conditions were first identified with synthetic media, where a product concentration of 9.9 g L-1 L-GalOA was obtained with a product selectivity of 99% (L-GalOA D-GalA-1) at pH 5 with 4% (w/v) sorbitol within 48 h. A very similar batch process performance with a product selectivity of 97% was achieved with potassium citrate buffered SBPP hydrolysate, demonstrating for the first time direct production of L-GalOA from hydrolyzed biomass using engineered S. cerevisiae. Combining the hydrolysis process of extracted SBPP and the biotransformation process with engineered S. cerevisiae paves the way towards repurposing pectin-rich residues as substrates for value-added chemicals.
As a flavor and platform chemical, m-cresol (3-methylphenol) is a valuable industrial compound that currently is mainly synthesized by chemical methods from fossil resources. In this study, we present the first biotechnological de novo production of m-cresol from sugar in complex yeast extract-peptone medium with the yeast Saccharomyces cerevisiae. A heterologous pathway based on the decarboxylation of the polyketide 6-methylsalicylic acid (6-MSA) was introduced into a CEN.PK yeast strain. For synthesis of 6-MSA, expression of different variants of 6-MSA synthases (MSASs) were compared. Overexpression of codon-optimized MSAS from Penicillium patulum together with activating phosphopantetheinyl transferase npgA from Aspergillus nidulans resulted in up to 367 mg/L 6-MSA production. Additional genomic integration of the genes had a strongly promoting effect and 6-MSA titers reached more than 2 g/L. Simultaneous expression of 6-MSA decarboxylase patG from A. clavatus led to the complete conversion of 6-MSA and production of up to 589 mg/L m-cresol. As addition of 450–750 mg/L m-cresol to yeast cultures nearly completely inhibited growth our data suggest that the toxicity of m-cresol might be the limiting factor for higher production titers.
Background: The production of bioethanol from lignocellulose hydrolysates requires a robust, D-xylose-fermenting and inhibitor-tolerant microorganism as catalyst. The purpose of the present work was to develop such a strain from a prime industrial yeast strain, Ethanol Red, used for bioethanol production.
Results: An expression cassette containing 13 genes including Clostridium phytofermentans XylA, encoding D-xylose isomerase (XI), and enzymes of the pentose phosphate pathway was inserted in two copies in the genome of Ethanol Red. Subsequent EMS mutagenesis, genome shuffling and selection in D-xylose-enriched lignocellulose hydrolysate, followed by multiple rounds of evolutionary engineering in complex medium with D-xylose, gradually established efficient D-xylose fermentation. The best-performing strain, GS1.11-26, showed a maximum specific D-xylose consumption rate of 1.1 g/g DW/h in synthetic medium, with complete attenuation of 35 g/L D-xylose in about 17 h. In separate hydrolysis and fermentation of lignocellulose hydrolysates of Arundo donax (giant reed), spruce and a wheat straw/hay mixture, the maximum specific D-xylose consumption rate was 0.36, 0.23 and 1.1 g/g DW inoculum/h, and the final ethanol titer was 4.2, 3.9 and 5.8% (v/v), respectively. In simultaneous saccharification and fermentation of Arundo hydrolysate, GS1.11-26 produced 32% more ethanol than the parent strain Ethanol Red, due to efficient D-xylose utilization. The high D-xylose fermentation capacity was stable after extended growth in glucose. Cell extracts of strain GS1.11-26 displayed 17-fold higher XI activity compared to the parent strain, but overexpression of XI alone was not enough to establish D-xylose fermentation. The high D-xylose consumption rate was due to synergistic interaction between the high XI activity and one or more mutations in the genome. The GS1.11-26 had a partial respiratory defect causing a reduced aerobic growth rate.
Conclusions: An industrial yeast strain for bioethanol production with lignocellulose hydrolysates has been developed in the genetic background of a strain widely used for commercial bioethanol production. The strain uses glucose and D-xylose with high consumption rates and partial cofermentation in various lignocellulose hydrolysates with very high ethanol yield. The GS1.11-26 strain shows highly promising potential for further development of an all-round robust yeast strain for efficient fermentation of various lignocellulose hydrolysates.
Die mitochondriale Innenmembran (IM) besteht aus zwei Subkompartimenten. Der
Cristae Membran (CM) und der inneren Grenzmembran (IBM), welche durch die runden und
schlitzartige Strukturen der Christa Junctions (CJs) verbunden werden Der MICOS-Komplex
ist an den CJs lokalisiert und besteht aus mindestens 6 Komponenten, Mic60, Mic27, Mic26,
Mic19, Mic12 und Mic10. Es ist bekannt, dass der MICOS-Komplex essentiell für die Stabilität der CJs ist. Die in dieser Arbeit gezeigten Ergebnisse, geben Aufschluss darüber, wie sich
einzelne MICOS-Komponenten auf die Stabilität von Cristae und CJs im Modellsystem Hefe (S
cerevisiae) auswirken. Zu Beginn dieser Arbeit war zum einen bekannt, dass die MICOSKomponente
Mic60 essentiell für die Bildung von CJs ist. Zum Anderen wurden im Vorfeld
dieser Arbeit Interaktionen von Mic60 mit Proteinen in der mitochondrialen Außenmembran,
vor allem Proteinkomplexe mit ȕ-barrel-Proteinen identifiziert. Diese Interaktionen werden
über den evolutionär, konservierten C-Terminus von Mic60 vermittelt.
ȕ-barrel Proteine besitzen eine charakteristische Peptidsequenz, die ȕ-Sequenz. Diese
dient nach dem Import der ȕ-barrel Proteine in die Mitochondrien als Signalpeptid für den
SAM-/TOB-Komplex, welcher daraufhin die Proteine in die Außenmembran insertiert. In
dieser Arbeit wurde ebenfalls eine ȕ-Sequenz im C-Terminus von Mic60 identifiziert, diese
zeigte einen Einfluss auf die Cristae-Stabilität. Zellen die eine Mic60-Variante mit einer
Deletion oder Punktmutation der ȕ- Domäne exprimieren, zeigten eine reduzierte Anzahl an
CJs. Auch das Verkürzen des C-Terminus von Mic60 hatte diesen Effekt auf die mitochondriale
Ultrastruktur. So konnte gezeigt werden, dass die ȕ-Domäne und die Integrität des C-Terminus
essentiell für die Stabilität von CJs sind.
Der Fokus dieser Arbeit lag in der Charakterisierung der MICOS-Komponenten Mic26
und Mic27. Es konnte bewiesen werden, dass beide Proteine genetisch mit der MICOSKernkomponente
Mic60 interagieren. Die Untersuchung der mitochondrialen Ultrastruktur von
Δmicβ6- und Δmicβ7-Zellen zeigte, dass eine Deletion vom Mic26 keinen Einfluss auf die
Organisation der mitochondrialen Innenmembran hat. Im Gegensatz dazu, ist im Vergleich zum
Wildtyp die Anzahl an CJs in Δmicβ7-Zellen um zwei Drittel reduziert. Auch die
Innenmembranoberfläche ist in diesen Zellen stark vergrößert. Die Untersuchung der
Morphologie der mitochondrialen Innenmembran in Zellen ohne Mic27 durch KryoElektronentomographie
isolierter Mitochondrien, veranschaulichte die Struktur der CJs in
diesen Zellen genauer. Es zeigten sich hier breitere CJs, und der Übergang von der
Cristaemembran in den Bereich der inneren Grenzmembran ist sehr flach und undefiniert. In
Wildtyp-Mitochondrien waren die CJs schmal und schlitzartig und haben einen scharfkantigen
Übergang von der Cristaemembran zur inneren Grenzmembran. Des Weiteren wies die
Cristaemembran in Δmicβ7-Zellen unregelmäßige zackige Strukturelemente auf, was auf eine
Anhäufung an Dimeren der F1FO-ATP Synthase hinweist.
Diese Beobachtungen in den Kryo-Tomogrammen, wurde durch Analysen des sich deutlich weniger höhere Oligomere und vermehrt Dimere. So kann aus diesen Befunden
geschlossen werden, dass Mic27 die Oligomere der F1FO-ATP Synthase stabilisiert.
Um zu untersuchen, wie der MICOS-Komplex mit der F1FO-ATP Synthase in
Verbindung steht, wurde mittels 2D-BNE-Analysen und einem Complexome Profiling die
Komplexierung der nativen Komplexe in Wildtyp- und Δmicβ7-Mitochondrien analysiert. Zum
einen konnte durch diese Untersuchungen gezeigt werden, dass Mic27 neben der F1FO-ATP
Synthase auch stabilisierend auf den MICOS-Komplex wirkt. Die Komplexe im
hochmolekularen Bereich der MICOS-Komponenten zerfielen in Δmicβ7-Zellen, was darauf
hinweist, dass die anderen MICOS-Komponenten hier nicht mehr assemblieren können. Mic10
war die einzige MICOS-Komponente die in Δmicβ7-Zellen noch stabile Komplexe im hohen
Massenbereich ausbildete. Mic10 findet sich zudem nicht nur in Klustern mit anderen MICOSKomponenten
sondern auch mit der F1FO-ATP Synthase.
Die Interaktion von Mic10 und der F1FO-ATP Synthase wurde auch biochemisch,
mittels chemischer Quervernetzern und Ko-Immunpräzipitationsexperimenten bestätigt. Dies
legt nahe, dass Mic10 die CJs mit hoher Wahrscheinlichkeit, durch die Verbindung mit der
F1FO-ATP Synthase, mit der Cristaemembran verbindet und so stabilisiert.
Aufgrund der Erkenntnisse dieser Arbeit konnte ein neuartiges Modell postuliert
werden. Die MICOS-Komponente Mic60 stabilisiert die CJs durch eine Interaktion seines CTerminus
mit Proteinen in der Außenmembran. Mic27 vermittelt über Mic10 die Interaktion
zur F1FO-ATP Synthase. Somit ist diese neu identifizierte Interaktion des MICOS-Komplex zur
F1FO-ATP Synthase essentiell für die Stabilität von CJs ist, indem es den MICOS-Komplex mit
den Oligomeren der F1FO-ATP Synthase verbindet.
Oligomerisierungszustands der F1FO-ATP Synthase in Δmicβ7-Zellen, bestätigt. Hier fanden
sich deutlich weniger höhere Oligomere und vermehrt Dimere. So kann aus diesen Befunden
geschlossen werden, dass Mic27 die Oligomere der F1FO-ATP Synthase stabilisiert.
Um zu untersuchen, wie der MICOS-Komplex mit der F1FO-ATP Synthase in
Verbindung steht, wurde mittels 2D-BNE-Analysen und einem Complexome Profiling die
Komplexierung der nativen Komplexe in Wildtyp- und Δmicβ7-Mitochondrien analysiert. Zum
einen konnte durch diese Untersuchungen gezeigt werden, dass Mic27 neben der F1FO-ATP
Synthase auch stabilisierend auf den MICOS-Komplex wirkt. Die Komplexe im
hochmolekularen Bereich der MICOS-Komponenten zerfielen in Δmicβ7-Zellen, was darauf
hinweist, dass die anderen MICOS-Komponenten hier nicht mehr assemblieren können. Mic10
war die einzige MICOS-Komponente die in Δmicβ7-Zellen noch stabile Komplexe im hohen
Massenbereich ausbildete. Mic10 findet sich zudem nicht nur in Klustern mit anderen MICOSKomponenten
sondern auch mit der F1FO-ATP Synthase.
Die Interaktion von Mic10 und der F1FO-ATP Synthase wurde auch biochemisch,
mittels chemischer Quervernetzern und Ko-Immunpräzipitationsexperimenten bestätigt. Dies
legt nahe, dass Mic10 die CJs mit hoher Wahrscheinlichkeit, durch die Verbindung mit der
F1FO-ATP Synthase, mit der Cristaemembran verbindet und so stabilisiert.
Aufgrund der Erkenntnisse dieser Arbeit konnte ein neuartiges Modell postuliert
werden. Die MICOS-Komponente Mic60 stabilisiert die CJs durch eine Interaktion seines CTerminus
mit Proteinen in der Außenmembran. Mic27 vermittelt über Mic10 die Interaktion
zur F1FO-ATP Synthase. Somit ist diese neu identifizierte Interaktion des MICOS-Komplex zur
F1FO-ATP Synthase essentiell für die Stabilität von CJs ist, indem es den MICOS-Komplex mit
den Oligomeren der F1FO-ATP Synthase verbindet.
For thousands of years, S. cerevisiae has been employed by humans in brewing and baking. Nowadays, this budding yeast is more than that: it is a well investigated model organism and an established workhorse in biotechnology. S. cerevisiae serves as a production host for various applications such as i) bioethanol production ii) the biosynthesis of hormones including insulin or iii) cannabinoid biosynthesis. Hereby, the robustness of S. cerevisiae and its high tolerances regarding pH and salt concentrations qualifies it for a wide range of industrial applications. Moreover, products of S. cerevisiae are generally recognised as safe (GRAS), enabling diverse biotechnological applications. Various mechanisms for genetic engineering of S. cerevisiae are applicable and the engineering process itself is straightforward since methods are established and widely known. Due to the wide range of industrial applications of S. cerevisiae, this organism is an ideal candidate for applied research and implementation of the recombinant biosynthesis of tocochromanols in this study.
Tocochromanols encompass tocotrienols and tocopherols, which are lipid-soluble compounds that are commonly associated with vitamin E activity. Hereby, α-tocopherol is the most prevalent form, as it is an essential nutrient in the diet of humans and animals. Naturally, tocochromanols are almost exclusively synthesised by photoautotrophic organisms such as plants or cyanobacteria. They consist of an aromatic head group and a polyprenyl side chain which is saturated in tocopherols and 3-fold unsaturated in tocotrienols. The methylation status of the chromanol ring distinguishes α-, β-, γ- and δ-tocochromanol. All forms of tocochromanols represent a group of powerful antioxidants, scavenging reactive oxygen species (ROS) and preventing the propagation of lipid oxidation in lipophilic environments. Recently, attention has been drawn to tocotrienols, due to their benefits in neuroprotection as well as cholesterol-lowering and anti-cancer properties. Consequently, tocochromanols are valuable additives in the food, feed, cosmetic and pharmaceutical industries.
The metabolic engineering strategy of S. cerevisiae to enable tocochromanol biosynthesis was started in a preceding master thesis with the provision of the aromatic moiety, homogentisic acid (HGA), from the aromatic amino acid biosynthesis. Hereby, the upregulation and redirection of the native pathway was essential. Therefore, a strain with an engineered aromatic amino acid pathway for improved 4 hydroxyphenylpyruvate (HPP) production (MRY33) was utilised from Reifenrath and Boles (2018). Furthermore, a heterologous hydroxyphenylpyruvate dioxygenase (HPPD) was required to convert HPP into HGA. Thus, several heterologous HPPDs were expressed and characterised regarding their HGA production within the previous study. The best variant originated from Yarrowia lipolytica, YlHPPD, and was integrated into the genome of MRY33. The resulting strain JBY2, produced 435 mg/L HGA in a shake flask fermentation.
This work was started with the genetically highly modified strain JBY2, whose genome already contained a large number of genes artificially expressed behind strong promoters. For further strain development, it was advantageous to maintain a high degree of sequence variability in order to prevent genomic instabilities due to sequence homologies. Thus, 17 artificial promoters (AP1-AP17) were characterised regarding their strength of expression by the yellow fluorescent protein (YFP). These sequences were also part of a patent that was filed during this work (WO2023094429A1).
The key point of this study was the development of a metabolic engineering strategy for the strain JBY2. First, the sufficient supply of the second precursor, the polyprenyl side chain, was investigated. Natively, S. cerevisiae produces the precursor, geranylgeranyl diphosphate (GGPP), from the isopentenyl diphosphate pathway. However, without further engineering, GGPP was barely detectable in JBY2 (< 0.1 mg/L). Thus, engineering of the isopentenyl diphosphate biosynthesis was necessary. The limiting enzyme of the mevalonate pathway was the 3-hydroxy-3-methylglutaryl coenzyme A reductase (HMGCR), which is encoded by HMG1. Therefore, a truncation for feedback-resistance and its overexpression by a promoter exchange was performed. Furthermore, the promoter of the gene for the squalene synthase (pERG9) was exchanged by the ergosterol sensitive promoter pERG1 to limit the metabolic flux of the mevalonate pathway into the ergosterol pathway. The native GGPP synthase (BTS1) was another limitation that was observed throughout this study. To overcome this bottleneck, plasmid-based and integrative overexpression of the native BTS1 and a codon optimised BTS1 were investigated. Other strategies to improve GGPP production were the deletion of the gene for the diacylglycerol pyrophosphate phosphatase (DPP1) to prevent excessive dephosphorylation of GGPP to geranylgeraniol (GGOH), and the overexpression of the farnesyl pyrophosphate synthetase, encoded by ERG20. However, the best improvements of the GGPP biosynthesis, inferred through GGOH measurements, were achieved from the screening of several heterologous GGPP synthases in S. cerevisiae. The best performing strain was JBY61 (JBY2, hmg1Δ::pTDH3-HMG1tr[1573–3165], pERG9Δ::pERG1, ChrIV-49293-49345Δ::pTDH3-XdcrtE-tSSA1_LEU2), bearing the heterologous GGPP synthase crtE of Xanthophyllomyces dendrorhous and produced 64.23 mg/L GGOH. Consequently, this engineering strategy improved the GGOH production by a factor of 642 compared to the parent strain JBY2.
In Europe, the sugar refinery is largely based on sugar beets. This route for obtaining household sugar results in a large amount of biomass waste, consisting mainly of the insoluble beet resi-dues, e.g., cell wall fragments. To a vast moiety this debris consists of the polymer pectin (up to 20% in the dry total solids). The structure of pectin is based on a backbone of D-galacturonic acid units (GalA), but also contains various other sugar monomers, predominantly L-arabinose, D-galactose, L-rhamnose and D-xylose. The amount of GalA adds up to a moiety of up to 70% with-in this sugar cocktail. So far, this debris is only fed to cattle or simply burnt. In nature, pectin is a common substrate for various organisms. The degradation of pectin-rich biomass is often per-formed by filamentous fungi like Hypocrea jecorina (also known as Trichoderma reesei) and As-pergillus niger, which evolved pectinases to degrade the pectin backbone and pathways to con-sume the monomer GalA as a sole carbon source. The fungal catabolism of pectin residues starts with the reduction of GalA to L-galactonate (GalOA) by a GalA-reductase. Even though filamen-tous fungi are native hosts of the GalA-catabolism and certain engineering approaches have al-ready been demonstrated, this class of organisms remains challenging with regard to bioreactor cultivation and tedious genetic accessibility. In contrast, the yeast S. cerevisiae is well known in fermentation processes and easily modified by a versatile set of genetic tools. So far, first ap-proaches have already been conducted to transfer the GalA utilization pathways into S. cerevisiae, but these approaches indicated limitations regarding GalA-uptake and redox cofac-tor replenishment due to the relatively high oxidative state of GalA compared to other sugars like glucose and galactose. Furthermore, the generally strongly increased demand for redox co-factors must be met by GalA reduction by finding new cofactor sources or redirecting reactions of the core metabolism.
This work aimed at the production of GalOA, which is the first intermediate of the fungal GalA catabolism. This compound shows an interesting range of potential applications, for instance as a food and cosmetic additive. To overcome the oxidized character of GalA, the presence of a more reduced co-substrate as a redox donor and as a carbon and energy source was required. To further enhance the reduction of GalA, modulation of the redox-cofactor supply and enzyme engineering were performed.
A promising strategy to reduce the dependency from fossil fuels is to use the yeast Saccharomyces cerevisiae to bioconvert renewable non-food feedstocks or waste streams, like lignocellulosic biomass, into bioethanol and other valuable molecule blocks. Lignocellulosic feedstocks contain glucose and significant fractions of the pentoses xylose and arabinose in varying proportions depending on the biomass type. S. cerevisiae is an efficient glucose consumer, but it cannot metabolize xylose and arabinose naturally. Therefore, extensive research using recombinant DNA techniques has been conducted to introduce and improve the biochemical pathways necessary to utilize these non-physiological substrates. However, any functional pathway capable of metabolizing D xylose and L arabinose in S. cerevisiae requires the transport of these sugars across the plasma membrane. The endogenous sugar transport system of S. cerevisiae can conduct a limited uptake of D-xylose and L-arabinose; this uptake enables only basal growth when the enzymatic pathways are provided. For this reason, the uptake of D xylose and L-arabinose has been recognized as a limiting step for the efficient utilization of these non-physiological substrates.
Gal2, a member of the major facilitator superfamily, is one of the most studied hexose transporters in S. cerevisiae. Although its expression is repressed in the presence of glucose, it also transports this sugar with high affinity when constitutively expressed. Recent efforts to engineer yeast strains for the utilization of plant biomass have unraveled the ability of Gal2 to transport non-physiological substrates like xylose and arabinose, among others. Improving Gal2 kinetic and substrate specificity, particularly for pentoses, has become a crucial target in strain engineering. The main goal of this study is to improve the utilization of xylose and arabinose by increasing the cell permeability of these non physiological substrates through the engineering of the galactose permease Gal2.
GAL2 gene expression depends on galactose, which acts as an inducer; nevertheless, even in the presence of galactose, glucose act as a strict repressor; consequently, GAL2 gene is usually placed under the control of a constitutive promoter. However, the presence of glucose additionally triggers the Gal2 degradation, which is mediated by the covalent attachment of the small 76 amino acid protein ubiquitin (Ub) to the targeted transporter; in a multi-step process called ubiquitination.
Ubiquitination of hexose permeases involves the activation of the Ub molecule by the E1 Ub-activating enzyme using ATP; then, the activated Ub is transferred to a specific Ub-conjugating enzyme E2, which donates the Ub indirectly through a specific HECT E3 enzyme (Rsp5) to a lysine residue of the substrate, with the aid of an adaptor protein which recognizes the target (Rsp5-adaptor). Ubiquitinated permeases are sent by membrane invagination to early endosomes, where they encounter ESCRTs (endosomal sorting complex required for transport). The targeted permeases are sorted in intralumenal vesicles (ILV) inside of the endosome, which after several cycles, turns into a multivesicular body (MVB) that subsequently fuses with the vacuole to expose the protein content of the ILVs to lumenal hydrolases for degradation.
Gal2 contains 30 lysine residues that may accept the ubiquitin molecule, which targets its degradation. It is known that mono-ubiquitination by Rsp5 on multiple lysine residues is necessary to internalize Gal2 (Horak & Wolf, 2001). However, the authors did not identify the specific lysine residues involved in the ubiquitination processes. This study screened several Gal2 variants where lysine residues were mutated or removed from the protein sequence to discover which lysine residues are likely involved in ubiquitination and consequent turnover of the transporter. The results of the screening showed that mutation of the N terminal lysine residues 27, 37, and 44 to arginine (Gal23KR) produced a functional transporter that, when fused with GFP (Gal23KR_GFP), showed an exclusive localization at the plasma membrane in cells growing in galactose or glucose as a sole carbon source (Tamayo Rojas et al., 2021b).
This study furthermore evaluated upstream signals caused by phosphorylation which triggers ubiquitination and consequent turnover of the targeted protein; using similar screening approaches to assess the stabilization of Gal2 by lysine residue modifications, it was possible to identify that N terminal serine residues 32, 35, 39, 48, 53, and 55 are likely involved in the internalization of Gal2, since a Gal2 construct where all these serines were mutated to alanine residues and tagged with GFP (Gal26SA_GFP) exhibited practically complete localization at the plasma membrane in cells growing in galactose or glucose as a sole carbon source (Tamayo Rojas et al., 2021b)...
FAD synthase is the last enzyme in the pathway that converts riboflavin into FAD. In Saccharomyces cerevisiae, the gene encoding for FAD synthase is FAD1, from which a sole protein product (Fad1p) is expected to be generated. In this work, we showed that a natural Fad1p exists in yeast mitochondria and that, in its recombinant form, the protein is able, per se, to both enter mitochondria and to be destined to cytosol. Thus, we propose that FAD1 generates two echoforms—that is, two identical proteins addressed to different subcellular compartments. To shed light on the mechanism underlying the subcellular destination of Fad1p, the 3′ region of FAD1 mRNA was analyzed by 3′RACE experiments, which revealed the existence of (at least) two FAD1 transcripts with different 3′UTRs, the short one being 128 bp and the long one being 759 bp. Bioinformatic analysis on these 3′UTRs allowed us to predict the existence of a cis-acting mitochondrial localization motif, present in both the transcripts and, presumably, involved in protein targeting based on the 3′UTR context. Here, we propose that the long FAD1 transcript might be responsible for the generation of mitochondrial Fad1p echoform.