Efficient secretion of two fungal cellobiohydrolases by Saccharomyces cerevisiae

Two different cellobiohydrolases, CBHI and CBHII, of the filamentous fungus Trichoderma reesei both hydrolyse highly crystalline cellulose. Cellulolytic strains of the yeast Saccharomyces cerevisiae were constructed by transferring cDNAs coding for these enzymes into yeast on an expression plasmid. These cellulolytic yeasts were able to secrete efficiently the large, heterologous proteins to the culture medium. The recombinant cellulases were observed to be heterogeneous in Mr due, at least partly, to variable N-glycosylation. Recombinant CBHII was able to bind to crystalline cellulose, although slightly less efficiently than the native enzyme. Both of the two recombinant cellulases were able to degrade amorphous cellulose. In a fermenter cultivation, around 100 micrograms/ml of CBHII was secreted into the yeast growth medium.     

Cloning, expression, and characterization of novel thermostable family 7 cellobiohydrolases

As part of the effort to find better cellulases for bioethanol production processes, we were looking for novel GH-7 family cellobiohydrolases, which would be particularly active on insoluble polymeric substrates and participate in the rate-limiting step in the hydrolysis of cellulose. The enzymatic properties were studied and are reported here for family 7 cellobiohydrolases from the thermophilic fungi Acremonium thermophilum, Thermoascus aurantiacus, and Chaetomium thermophilum. The Trichoderma reesei Cel7A enzyme was used as a reference in the experiments. As the native T. aurantiacus Cel7A has no carbohydrate-binding module (CBM), recombinant proteins having the CBM from either the C. thermophilum Cel7A or the T. reesei Cel7A were also constructed. All these novel acidic cellobiohydrolases were more thermostable (by 4-10 degrees C) and more active (two- to fourfold) in hydrolysis of microcrystalline cellulose (Avicel) at 45 degrees C than T. reesei Cel7A. The C. thermophilum Cel7A showed the highest specific activity and temperature optimum when measured on soluble substrates. The most effective enzyme for Avicel hydrolysis at 70 degrees C, however, was the 2-module version of the T. aurantiacus Cel7A, which was also relatively weakly inhibited by cellobiose. These results are discussed from the structural point of view based on the three-dimensional homology models of these enzymes.     

Recombinant thermostable cycloinulo-oligosaccharide fructanotransferase produced by Saccharomyces cerevisiae.

A truncated fragment of the cycloinulo-oligosaccharide fructanotransferase (CFTase) gene of Bacillus circulans MCI-2554 was fused to the prepro secretion sequence of the alpha-factor and expressed in Saccharomyces cerevisiae under the control of the 5' upstream region of the isocitrate lyase gene of Candida tropicalis (UPR-ICL). Efficiently secreted recombinant CFTase protein (yeast CFTase) was purified. Yeast CFTase consisted of three protein molecules, each of which had CFTase activity (yeast CFTase 1 [116 kDa], yeast CFTase 2 [117 kDa], and yeast CFTase 3 [116 kDa]). Yeast CFTase 2 was the major product of the expression system employed and was shown to be N glycosylated by endoglycosidase H treatment. Yeast CFTase 1 was N glycosylated but had a short truncation at its N terminus, while yeast CFTase 3 did not contain an N-glycosylated carbohydrate chain(s). Yeast CFTase 2 showed an optimum pH, an optimum temperature, and a pH stability similar to those of CFTase purified from B. circulans but exhibited a significant increase in thermostability. Production of yeast CFTase by the strain which had two copies of the CFTase gene integrated into its chromosomes reached 391 U per liter of culture at 120 h, which corresponded to 8.40 mg of protein per liter, by shake-flask cultivation.     

Metabolic Engineering of Saccharomyces cerevisiae

Comprehensive knowledge regarding Saccharomyces cerevisiae has accumulated over time, and today S. cerevisiae serves as a widley used biotechnological production organism as well as a eukaryotic model system. The high transformation efficiency, in addition to the availability of the complete yeast genome sequence, has facilitated genetic manipulation of this microorganism, and new approaches are constantly being taken to metabolicially engineer this organism in order to suit specific needs. In this paper, strategies and concepts for metabolic engineering are discussed and several examples based upon selected studies involving S. cerevisiae are reviewed. The many different studies of metabolic engineering using this organism illustrate all the categories of this multidisciplinary field: extension of substrate range, improvements of producitivity and yield, elimination of byproduct formation, improvement of process performance, improvements of cellular properties, and extension of product range including heterologous protein production.     

Recombinational instability of a chimeric plasmid in Saccharomyces cerevisiae.

Wild-type strains of Saccharomyces cerevisiae exhibit mitotic recombination between the chimeric plasmid TLC-1 and the endogenous 2mu circle that involves sequence homologies between the two plasmids that are not acted on by the 2mu circle site-specific recombination system. This generalized recombination can be detected because it separates the LEU2 and CAN1 markers of TLC-1 from each other through the formation of a plasmid containing only the S. cerevisiae LEU2 region and the 2mu circle. This derivative plasmid is maintained more stably during vegetative growth than TLC-1, and strains which carry it frequently lose the endogenous 2mu circle. Therefore, TLC-1 can provide a convenient selection for [cir0] cells. Formation of this new plasmid is greatly reduced, but not eliminated, in strains containing the rad52-1 mutation. This indicates that generalized mitotic recombination between plasmid sequences utilizes functions required for chromosomal recombination in S. cerevisiae.     

Engineering oxygen-independent biotin biosynthesis in Saccharomyces cerevisiae

An oxygen requirement for de novo biotin synthesis in Saccharomyces cerevisiae precludes the application of biotin-prototrophic strains in anoxic processes that use biotin-free media. To overcome this issue, this study explores introduction of the oxygen-independent Escherichia coli biotin-biosynthesis pathway in S. cerevisiae. Implementation of this pathway required expression of seven E. coli genes involved in fatty-acid synthesis and three E. coli genes essential for the formation of a pimelate thioester, key precursor of biotin synthesis. A yeast strain expressing these genes readily grew in biotin-free medium, irrespective of the presence of oxygen. However, the engineered strain exhibited specific growth rates 25% lower in biotin-free media than in biotin-supplemented media. Following adaptive laboratory evolution in anoxic cultures, evolved cell lines that no longer showed this growth difference in controlled bioreactors, were characterized by genome sequencing and proteome analyses. The evolved isolates exhibited a whole-genome duplication accompanied with an alteration in the relative gene dosages of biosynthetic pathway genes. These alterations resulted in a reduced abundance of the enzymes catalyzing the first three steps of the E. coli biotin pathway. The evolved pathway configuration was reverse engineered in the diploid industrial S. cerevisiae strain Ethanol Red. The resulting strain grew at nearly the same rate in biotin-supplemented and biotin-free media non-controlled batches performed in an anaerobic chamber. This study established an unique genetic engineering strategy to enable biotin-independent anoxic growth of S. cerevisiae and demonstrated its portability in industrial strain backgrounds.     

构建酿酒酵母工程菌合成香紫苏醇

香紫苏醇是一种来源于植物的双环二萜醇,常用于香味成分且具有重要生物学活性。为实现香紫苏醇的微生物生产,以酿酒酵母为宿主,表达焦磷酸赖百当烯二醇酯合酶和香紫苏醇合酶,构建香紫苏醇的人工生物合成途径。发现过表达前体代谢关键酶、蛋白质融合增强底物通道效应及去除异源蛋白信号肽等,有利于香紫苏醇合成。在摇瓶培养条件下,组合优化得到的工程菌株S6的香紫苏醇产量达到8.96 mg/L。研究结果对其他萜类化合物的异源生物合成具有参考价值。     

Engineering Saccharomyces cerevisiae for isoprenol production

Isoprenol (3-methyl-3-butene-1-ol) is a valuable drop-in biofuel and an important precursor of several commodity chemicals. Synthetic microbial systems using the heterologous mevalonate pathway have recently been developed for the production of isoprenol in Escherichia coli, and a significant yield and titer improvement has been achieved through a decade of research. Saccharomyces cerevisiae has been widely used in the biotechnology industry for isoprenoid production, but there has been no good example of isoprenol production reported in this host. In this study, we engineered the budding yeast S. cerevisiae for improved biosynthesis of isoprenol. The strain engineered with the mevalonate pathway achieved isoprenol production at the titer of 36.02 ± 0.92 mg/L in the flask. The IPP (isopentenyl diphosphate)-bypass pathway, which has shown more efficient isoprenol production by avoiding the accumulation of the toxic intermediate in E. coli, was also constructed in S. cerevisiae and improved the isoprenol titer by 2-fold. We further engineered the strains by deleting a promiscuous endogenous kinase that could divert the pathway flux away from the isoprenol production and improved the titer to 130.52 ± 8.01 mg/L. Finally, we identified a pathway bottleneck using metabolomics analysis and overexpressed a promiscuous alkaline phosphatase to relieve this bottleneck. The combined efforts resulted in the titer improvement to 383.1 ± 31.62 mg/L in the flask. This is the highest isoprenol titer up to date in S. cerevisiae and this work provides the key strategies to engineer yeast as an industrial platform for isoprenol production.     

Metabolic Engineering of Glycerol Production in Saccharomyces cerevisiae

Inactivation of TPI1, the Saccharomyces cerevisiae structural gene encoding triose phosphate isomerase, completely eliminates growth on glucose as the sole carbon source. In tpi1-null mutants, intracellular accumulation of dihydroxyacetone phosphate might be prevented if the cytosolic NADH generated in glycolysis by glyceraldehyde-3-phosphate dehydrogenase were quantitatively used to reduce dihydroxyacetone phosphate to glycerol. We hypothesize that the growth defect of tpi1-null mutants is caused by mitochondrial reoxidation of cytosolic NADH, thus rendering it unavailable for dihydroxyacetone-phosphate reduction. To test this hypothesis, a tpi1Δ nde1Δ nde2Δ gut2Δ quadruple mutant was constructed. NDE1 and NDE2 encode isoenzymes of mitochondrial external NADH dehydrogenase; GUT2 encodes a key enzyme of the glycerol-3-phosphate shuttle. It has recently been demonstrated that these two systems are primarily responsible for mitochondrial oxidation of cytosolic NADH in S. cerevisiae. Consistent with the hypothesis, the quadruple mutant grew on glucose as the sole carbon source. The growth on glucose, which was accompanied by glycerol production, was inhibited at high-glucose concentrations. This inhibition was attributed to glucose repression of respiratory enzymes as, in the quadruple mutant, respiratory pyruvate dissimilation is essential for ATP synthesis and growth. Serial transfer of the quadruple mutant on high-glucose media yielded a spontaneous mutant with much higher specific growth rates in high-glucose media (up to 0.10 h⁻¹ at 100 g of glucose·liter⁻¹). In aerated batch cultures grown on 400 g of glucose·liter⁻¹, this engineered S. cerevisiae strain produced over 200 g of glycerol·liter⁻¹, corresponding to a molar yield of glycerol on glucose close to unity.     

Engineered thermostable fungal Cel6A and Cel7A cellobiohydrolases hydrolyze cellulose efficiently at elevated temperatures

Thermostability is an important feature in industrial enzymes: it increases biocatalyst lifetime and enables reactions at higher temperatures, where faster rates and other advantages ultimately reduce the cost of biocatalysis. Here we report the thermostabilization of a chimeric fungal family 6 cellobiohydrolase (HJPlus) by directed evolution using random mutagenesis and recombination of beneficial mutations. Thermostable variant 3C6P has a half‐life of 280 min at 75°C and a T₅₀ of 80.1°C, a ～15°C increase over the thermostable Cel6A from Humicola insolens (HiCel6A) and a ～20°C increase over that from Hypocrea jecorina (HjCel6A). Most of the mutations also stabilize the less‐stable HjCel6A, the wild‐type Cel6A closest in sequence to 3C6P. During a 60‐h Avicel hydrolysis, 3C6P released 2.4 times more cellobiose equivalents at its optimum temperature (T_opt) of 75°C than HiCel6A at its T_opt of 60°C. The total cellobiose equivalents released by HiCel6A at 60°C after 60 h is equivalent to the total released by 3C6P at 75°C after ～6 h, a 10‐fold reduction in hydrolysis time. A binary mixture of thermostable Cel6A and Cel7A hydrolyzes Avicel synergistically and released 1.8 times more cellobiose equivalents than the wild‐type mixture, both mixtures assessed at their respective T_opt. Crystal structures of HJPlus and 3C6P, determined at 1.5 and 1.2 Å resolution, indicate that the stabilization comes from improved hydrophobic interactions and restricted loop conformations by introduced proline residues. Biotechnol. Bioeng. 2013; 110: 1874–1883. © 2013 Wiley Periodicals, Inc.     

Expression of a thermostable cellulase gene from a thermophilic anaerobe in Saccharomyces cerevisiae

A cellulase gene from a thermophilic anaerobe was recloned in the yeast Saccharomyces cerevisiae. The maximum level of the gene expression in the recombinant yeast was 4.4 times higher than that in the Escherichia coli transformant harboring the same plasmid. Cellulase activity was observed only within the yeast cells. To compare the enzymatic properties of cellulase produced by the yeast and E. coli transformants, cellulases were purified to homogeneous state by only three purification steps of heat treatment, and cellulose affinity and ion exchange chromatographies. The molecular weights of the enzymes produced by the yeast and E. coli were 3.8 × 10⁴ and 4.0 × 10⁴, respectively by SDS-polyacrylamide gel electrophoresis. Neither of the enzymes was glycosylated. Although the molecular weights were slightly different, enzymatic properties and thermostability were almost indistinguishable between the enzymes produced by the yeast and E. coli transformants.     

Engineering the biocatalytic selectivity of iridoid production in Saccharomyces cerevisiae

Monoterpene indole alkaloids (MIAs) represent a structurally diverse, medicinally essential class of plant derived natural products. The universal MIA building block strictosidine was recently produced in the yeast Saccharomyces cerevisiae, setting the stage for optimization of microbial production. However, the irreversible reduction of pathway intermediates by yeast enzymes results in a non-recoverable loss of carbon, which has a strong negative impact on metabolic flux. In this study, we identified and engineered the determinants of biocatalytic selectivity which control flux towards the iridoid scaffold from which all MIAs are derived. Development of a bioconversion based production platform enabled analysis of the metabolic flux and interference around two critical steps in generating the iridoid scaffold: oxidation of 8-hydroxygeraniol to the dialdehyde 8-oxogeranial followed by reductive cyclization to form nepetalactol. In vitro reconstitution of previously uncharacterized shunt pathways enabled the identification of two distinct routes to a reduced shunt product including endogenous ‘ene’-reduction and non-productive reduction by iridoid synthase when interfaced with endogenous alcohol dehydrogenases. Deletion of five genes involved in α,β-unsaturated carbonyl metabolism resulted in a 5.2-fold increase in biocatalytic selectivity of the desired iridoid over reduced shunt product. We anticipate that our engineering strategies will play an important role in the development of S. cerevisiae for sustainable production of iridoids and MIAs.     

Engineering the monomer composition of polyhydroxyalkanoates synthesized in Saccharomyces cerevisiae

Polyhydroxyalkanoates (PHAs) have received considerable interest as renewable-resource-based, biodegradable, and biocompatible plastics with a wide range of potential applications. We have engineered the synthesis of PHA polymers composed of monomers ranging from 4 to 14 carbon atoms in either the cytosol or the peroxisome of Saccharomyces cerevisiae by harnessing intermediates of fatty acid metabolism. Cytosolic PHA production was supported by establishing in the cytosol critical beta-oxidation chemistries which are found natively in peroxisomes. This platform was utilized to supply medium-chain (C6 to C14) PHA precursors from both fatty acid degradation and synthesis to a cytosolically expressed medium-chain-length (mcl) polymerase from Pseudomonas oleovorans. Synthesis of short-chain-length PHAs (scl-PHAs) was established in the peroxisome of a wild-type yeast strain by targeting the Ralstonia eutropha scl polymerase to the peroxisome. This strain, harboring a peroxisomally targeted scl-PHA synthase, accumulated PHA up to approximately 7% of its cell dry weight. These results indicate (i) that S. cerevisiae expressing a cytosolic mcl-PHA polymerase or a peroxisomal scl-PHA synthase can use the 3-hydroxyacyl coenzyme A intermediates from fatty acid metabolism to synthesize PHAs and (ii) that fatty acid degradation is also possible in the cytosol as beta-oxidation might not be confined only to the peroxisomes. Polymers of even-numbered, odd-numbered, or a combination of even- and odd-numbered monomers can be controlled by feeding the appropriate substrates. This ability should permit the rational design and synthesis of polymers with desired material properties.     

Engineering the Monomer Composition of Polyhydroxyalkanoates Synthesized in Saccharomyces cerevisiae

Polyhydroxyalkanoates (PHAs) have received considerable interest as renewable-resource-based, biodegradable, and biocompatible plastics with a wide range of potential applications. We have engineered the synthesis of PHA polymers composed of monomers ranging from 4 to 14 carbon atoms in either the cytosol or the peroxisome of Saccharomyces cerevisiae by harnessing intermediates of fatty acid metabolism. Cytosolic PHA production was supported by establishing in the cytosol critical β-oxidation chemistries which are found natively in peroxisomes. This platform was utilized to supply medium-chain (C₆ to C₁₄) PHA precursors from both fatty acid degradation and synthesis to a cytosolically expressed medium-chain-length (mcl) polymerase from Pseudomonas oleovorans. Synthesis of short-chain-length PHAs (scl-PHAs) was established in the peroxisome of a wild-type yeast strain by targeting the Ralstonia eutropha scl polymerase to the peroxisome. This strain, harboring a peroxisomally targeted scl-PHA synthase, accumulated PHA up to approximately 7% of its cell dry weight. These results indicate (i) that S. cerevisiae expressing a cytosolic mcl-PHA polymerase or a peroxisomal scl-PHA synthase can use the 3-hydroxyacyl coenzyme A intermediates from fatty acid metabolism to synthesize PHAs and (ii) that fatty acid degradation is also possible in the cytosol as β-oxidation might not be confined only to the peroxisomes. Polymers of even-numbered, odd-numbered, or a combination of even- and odd-numbered monomers can be controlled by feeding the appropriate substrates. This ability should permit the rational design and synthesis of polymers with desired material properties.     

啤酒酵母代谢工程研究进展

啤酒工业上应用的啤酒酵母菌株在生产中都会存在着某些方面的缺陷。通过分析啤酒酵母某些代谢产物的代谢途径,寻找改变其代谢流量的方法,然后用分子生物学手段对其代谢流量加以改变,来调节啤酒酵母某些产物的代谢水平已经成为啤酒酵母育种的新方式。对酵母的底物利用、可操作性、控制有害副产物的产量及改善啤酒风味等方面的研究成果进行了综述。     

Engineering redox cofactor regeneration for improved pentose fermentation in Saccharomyces cerevisiae

Pentose fermentation to ethanol with recombinant Saccharomyces cerevisiae is slow and has a low yield. A likely reason for this is that the catabolism of the pentoses D-xylose and L-arabinose through the corresponding fungal pathways creates an imbalance of redox cofactors. The process, although redox neutral, requires NADPH and NAD+, which have to be regenerated in separate processes. NADPH is normally generated through the oxidative part of the pentose phosphate pathway by the action of glucose-6-phosphate dehydrogenase (ZWF1). To facilitate NADPH regeneration, we expressed the recently discovered gene GDP1, which codes for a fungal NADP+-dependent D-glyceraldehyde-3-phosphate dehydrogenase (NADP-GAPDH) (EC 1.2.1.13), in an S. cerevisiae strain with the D-xylose pathway. NADPH regeneration through an NADP-GAPDH is not linked to CO2 production. The resulting strain fermented D-xylose to ethanol with a higher rate and yield than the corresponding strain without GDP1; i.e., the levels of the unwanted side products xylitol and CO2 were lowered. The oxidative part of the pentose phosphate pathway is the main natural path for NADPH regeneration. However, use of this pathway causes wasteful CO2 production and creates a redox imbalance on the path of anaerobic pentose fermentation to ethanol because it does not regenerate NAD+. The deletion of the gene ZWF1 (which codes for glucose-6-phosphate dehydrogenase), in combination with overexpression of GDP1 further stimulated D-xylose fermentation with respect to rate and yield. Through genetic engineering of the redox reactions, the yeast strain was converted from a strain that produced mainly xylitol and CO2 from D-xylose to a strain that produced mainly ethanol under anaerobic conditions.     

Evolutionary Engineering Improves Tolerance for Replacement Jet Fuels in Saccharomyces cerevisiae

Monoterpenes are liquid hydrocarbons with applications ranging from flavor and fragrance to replacement jet fuel. Their toxicity, however, presents a major challenge for microbial synthesis. Here we evolved limonene-tolerant Saccharomyces cerevisiae strains and sequenced six strains across the 200-generation evolutionary time course. Mutations were found in the tricalbin proteins Tcb2p and Tcb3p. Genomic reconstruction in the parent strain showed that truncation of a single protein (tTcb3p^1-989), but not its complete deletion, was sufficient to recover the evolved phenotype improving limonene fitness 9-fold. tTcb3p^1-989 increased tolerance toward two other monoterpenes (β-pinene and myrcene) 11- and 8-fold, respectively, and tolerance toward the biojet fuel blend AMJ-700t (10% cymene, 50% limonene, 40% farnesene) 4-fold. tTcb3p^1-989 is the first example of successful engineering of phase tolerance and creates opportunities for production of the highly toxic C₁₀ alkenes in yeast.