Engineering of Saccharomyces cerevisiae for efficient anaerobic alcoholic fermentation of L-arabinose

For cost-effective and efficient ethanol production from lignocellulosic fractions of plant biomass, the conversion of not only major constituents, such as glucose and xylose, but also less predominant sugars, such as l-arabinose, is required. Wild-type strains of Saccharomyces cerevisiae, the organism used in industrial ethanol production, cannot ferment xylose and arabinose. Although metabolic and evolutionary engineering has enabled the efficient alcoholic fermentation of xylose under anaerobic conditions, the conversion of l-arabinose into ethanol by engineered S. cerevisiae strains has previously been demonstrated only under oxygen-limited conditions. This study reports the first case of fast and efficient anaerobic alcoholic fermentation of l-arabinose by an engineered S. cerevisiae strain. This fermentation was achieved by combining the expression of the structural genes for the l-arabinose utilization pathway of Lactobacillus plantarum, the overexpression of the S. cerevisiae genes encoding the enzymes of the nonoxidative pentose phosphate pathway, and extensive evolutionary engineering. The resulting S. cerevisiae strain exhibited high rates of arabinose consumption (0.70 g h(-1) g [dry weight](-1)) and ethanol production (0.29 g h(-1) g [dry weight](-1)) and a high ethanol yield (0.43 g g(-1)) during anaerobic growth on l-arabinose as the sole carbon source. In addition, efficient ethanol production from sugar mixtures containing glucose and arabinose, which is crucial for application in industrial ethanol production, was achieved.     

酿酒酵母转化木糖生产化学品的研究进展

木糖的有效利用是木质纤维素生产生物燃料或化学品经济性转化的基础.30年来,通过理性代谢改造和适应性进化等工程策略,显著提高了传统乙醇发酵微生物——酿酒酵母Saccharomyces cerevisiae的木糖代谢能力.因此,近年来在酿酒酵母中利用木糖生产化学品的研究逐步展开.研究发现,酿酒酵母分别以木糖和葡萄糖为碳源时...     

Comparative study on a series of recombinant flocculent Saccharomyces cerevisiae strains with different expression levels of xylose reductase and xylulokinase

Ethanol production from xylose is important for the utilization of lignocellulosic biomass as raw materials. Recently, we reported the development of an industrial xylose-fermenting Saccharomyces cerevisiae strain, MA-R4, which was engineered by chromosomal integration to express the genes encoding xylose reductase and xylitol dehydrogenase from Pichia stipitis along with S. cerevisiae xylulokinase gene constitutively using the alcohol-fermenting flocculent yeast strain, IR-2. IR-2 has the highest xylulose-fermenting ability of the industrial diploid strains, making it a useful host strain for genetically engineering xylose-utilizing S. cerevisiae. To optimize the activities of xylose metabolizing enzymes in the metabolic engineering of IR-2 for further improvement of ethanol production from xylose, we constructed a set of recombinant isogenic strains harboring different combinations of genetic modifications present in MA-R4, and investigated the effect of constitutive expression of xylulokinase and of different levels of xylulokinase and xylose reductase activity on xylose fermentation. This strain comparison showed that constitutive expression of xylulokinase increased ethanol production from xylose at the expense of xylitol excretion, and that high activity of xylose reductase resulted in an increased rate of xylose consumption and an increased glycerol yield. Moreover, strain MA-R6, which has moderate xylulokinase activity, grew slightly better but accumulated more xylitol than strain MA-R4. These results suggest that fine-tuning of introduced enzyme activity in S. cerevisiae is important for improving xylose fermentation to ethanol.     

酿酒酵母戊糖转运蛋白及C6/C5共代谢菌株的研究进展

充分利用木质纤维素中的糖分是提高以此类生物质为原料生产二代燃料乙醇经济盈利性的基本要求,也是实现其他生物基化学品规模化生产的基础。传统的乙醇生产微生物酿酒酵母Saccharomyces cerevisiae具有独特的生产性能及内在优势,是备受关注的底盘细胞,但其不能有效地利用戊糖。利用代谢工程、合成生物学策略,对二代燃料乙醇生产专用酿酒酵母的精准构制持续研究了30余年,已明显改善了其对木糖/葡萄糖的乙醇共发酵能力。近年来关注点集中在早期忽略的限速步骤即糖转运环节的研究上,以期实现不同糖分各行其道、高效专一性转运蛋白各行其责的二代燃料乙醇生产特种酿酒酵母所需的糖转运理想状态。文中主要综述了酿酒酵母戊糖转运蛋白的研究进展,及酿酒酵母的木糖和L-阿拉伯糖代谢工程的研究现状。     

Engineering Saccharomyces cerevisiae for efficient anaerobic xylose fermentation: reflections and perspectives

Conversion of the abundant lignocellulosic biomass into ethanol is an environmentally sustainable solution to the energy crisis. Fermentation of lignocellulosic hydrolysates by Saccharomyces cerevisiae is not cost-effective yet as substantial amounts of xylose in the hydrolysates cannot be utilized by native S. cerevisiae strains. Extensive studies including both metabolic and evolutionary engineering have been carried out to develop an efficient xylose-fermenting S. cerevisiae strain, yet the ethanol yield and productivity from xylose fermentation of the best one are still far below expectation. This review compares the engineering approaches and resulted anaerobic xylose fermentation performance of recently reported xylose-utilizing S. cerevisiae strains, with the aim to understand the intrinsic reason for their low xylose fermentation capabilities. These comparative analyses revealed that some of the current engineering targets and the so-called "hot issues" might be overrated. Our opinions on the underrated parts and future efforts in this field are also presented. Overall, this review serves as a comprehensive reference to understanding xylose fermentation by S. cerevisiae.     

APJ1 and GRE3 homologs work in concert to allow growth in xylose in a natural Saccharomyces sensu stricto hybrid yeast

Creating Saccharomyces yeasts capable of efficient fermentation of pentoses such as xylose remains a key challenge in the production of ethanol from lignocellulosic biomass. Metabolic engineering of industrial Saccharomyces cerevisiae strains has yielded xylose-fermenting strains, but these strains have not yet achieved industrial viability due largely to xylose fermentation being prohibitively slower than that of glucose. Recently, it has been shown that naturally occurring xylose-utilizing Saccharomyces species exist. Uncovering the genetic architecture of such strains will shed further light on xylose metabolism, suggesting additional engineering approaches or possibly even enabling the development of xylose-fermenting yeasts that are not genetically modified. We previously identified a hybrid yeast strain, the genome of which is largely Saccharomyces uvarum, which has the ability to grow on xylose as the sole carbon source. To circumvent the sterility of this hybrid strain, we developed a novel method to genetically characterize its xylose-utilization phenotype, using a tetraploid intermediate, followed by bulk segregant analysis in conjunction with high-throughput sequencing. We found that this strain's growth in xylose is governed by at least two genetic loci, within which we identified the responsible genes: one locus contains a known xylose-pathway gene, a novel homolog of the aldo-keto reductase gene GRE3, while a second locus contains a homolog of APJ1, which encodes a putative chaperone not previously connected to xylose metabolism. Our work demonstrates that the power of sequencing combined with bulk segregant analysis can also be applied to a nongenetically tractable hybrid strain that contains a complex, polygenic trait, and identifies new avenues for metabolic engineering as well as for construction of nongenetically modified xylose-fermenting strains.     

Xylulokinase overexpression in two strains of Saccharomyces cerevisiae also expressing xylose reductase and xylitol dehydrogenase and its effect on fermentation of xylose and lignocellulosic hydrolysate

Fermentation of the pentose sugar xylose to ethanol in lignocellulosic biomass would make bioethanol production economically more competitive. Saccharomyces cerevisiae, an efficient ethanol producer, can utilize xylose only when expressing the heterologous genes XYL1 (xylose reductase) and XYL2 (xylitol dehydrogenase). Xylose reductase and xylitol dehydrogenase convert xylose to its isomer xylulose. The gene XKS1 encodes the xylulose-phosphorylating enzyme xylulokinase. In this study, we determined the effect of XKS1 overexpression on two different S. cerevisiae host strains, H158 and CEN.PK, also expressing XYL1 and XYL2. H158 has been previously used as a host strain for the construction of recombinant xylose-utilizing S. cerevisiae strains. CEN.PK is a new strain specifically developed to serve as a host strain for the development of metabolic engineering strategies. Fermentation was carried out in defined and complex media containing a hexose and pentose sugar mixture or a birch wood lignocellulosic hydrolysate. XKS1 overexpression increased the ethanol yield by a factor of 2 and reduced the xylitol yield by 70 to 100% and the final acetate concentrations by 50 to 100%. However, XKS1 overexpression reduced the total xylose consumption by half for CEN.PK and to as little as one-fifth for H158. Yeast extract and peptone partly restored sugar consumption in hydrolysate medium. CEN.PK consumed more xylose but produced more xylitol than H158 and thus gave lower ethanol yields on consumed xylose. The results demonstrate that strain background and modulation of XKS1 expression are important for generating an efficient xylose-fermenting recombinant strain of S. cerevisiae.     

Improved ethanol production by a xylose-fermenting recombinant yeast strain constructed through a modified genome shuffling method

ABSTRACT: BACKGROUND: Xylose is the second most abundant carbohydrate in the lignocellulosic biomass hydrolysate. The fermentation of xylose is essential for the bioconversion of lignocelluloses to fuels and chemicals. However the wild-type strains of Saccharomyces cerevisiae are unable to utilize xylose. Many efforts have been made to construct recombinant yeast strains to enhance xylose fermentation over the past few decades. Xylose fermentation remains challenging due to the complexity of lignocellulosic biomass hydrolysate. In this study, a modified genome shuffling method was developed to improve xylose fermentation by S. cerevisiae. Recombinant yeast strains were constructed by recursive DNA shuffling with the recombination of entire genome of P. stipitis with that of S. cerevisiae. RESULTS: After two rounds of genome shuffling and screening, one potential recombinant yeast strain ScF2 was obtained. It was able to utilize high concentration of xylose (100 g/L to 250 g/L xylose) and produced ethanol. The recombinant yeast ScF2 produced ethanol more rapidly than the naturally occurring xylose-fermenting yeast, P. stipitis, with improved ethanol titre and much more enhanced xylose tolerance. CONCLUSION: The modified genome shuffling method developed in this study was more effective and easier to operate than the traditional protoplast fusion based method. Recombinant yeast strain ScF2 obtained in this was a promising candidate for industrial cellulosic ethanol production. In order to further enhance its xylose fermentation performance, ScF2 needs to be additionally improved by metabolic engineering and directed evolution.     

辅酶工程在酿酒酵母木糖代谢工程中的研究进展

辅酶工程（cofactor engineering）是代谢工程的一个重要分支,它通过改变辅酶的再生途径,达到改变细胞内代谢产物构成的目的。介绍了酿酒酵母(Saccharomyces cerevisiae)木糖代谢工程中,利用辅酶工程解决氧化还原平衡问题的研究进展,包括引入转氢酶系统,增加代谢中可利用的NADPH,实现NADH的厌氧氧化等策略。同时介绍了改变XR、XDH辅酶偏好的研究进展。     

Increased ethanol productivity in xylose-utilizing Saccharomyces cerevisiae via a randomly mutagenized xylose reductase

Baker's yeast (Saccharomyces cerevisiae) has been genetically engineered to ferment the pentose sugar xylose present in lignocellulose biomass. One of the reactions controlling the rate of xylose utilization is catalyzed by xylose reductase (XR). In particular, the cofactor specificity of XR is not optimized with respect to the downstream pathway, and the reaction rate is insufficient for high xylose utilization in S. cerevisiae. The current study describes a novel approach to improve XR for ethanol production in S. cerevisiae. The cofactor binding region of XR was mutated by error-prone PCR, and the resulting library was expressed in S. cerevisiae. The S. cerevisiae library expressing the mutant XR was selected in sequential anaerobic batch cultivation. At the end of the selection process, a strain (TMB 3420) harboring the XR mutations N272D and P275Q was enriched from the library. The V(max) of the mutated enzyme was increased by an order of magnitude compared to that of the native enzyme, and the NADH/NADPH utilization ratio was increased significantly. The ethanol productivity from xylose in TMB 3420 was increased ～40 times compared to that of the parent strain (0.32 g/g [dry weight {DW}] × h versus 0.007 g/g [DW] × h), and the anaerobic growth rate was increased from ～0 h(-1) to 0.08 h(-1). The improved traits of TMB 3420 were readily transferred to the parent strain by reverse engineering of the mutated XR gene. Since integrative vectors were employed in the construction of the library, transfer of the improved phenotype does not require multicopy expression from episomal plasmids.     

Construction of a xylan-fermenting yeast strain through codisplay of xylanolytic enzymes on the surface of xylose-utilizing Saccharomyces cerevisiae cells

Hemicellulose is one of the major forms of biomass in lignocellulose, and its essential component is xylan. We used a cell surface engineering system based on alpha-agglutinin to construct a Saccharomyces cerevisiae yeast strain codisplaying two types of xylan-degrading enzymes, namely, xylanase II (XYNII) from Trichoderma reesei QM9414 and beta-xylosidase (XylA) from Aspergillus oryzae NiaD300, on the cell surface. In a high-performance liquid chromatography analysis, xylose was detected as the main product of the yeast strain codisplaying XYNII and XylA, while xylobiose and xylotriose were detected as the main products of a yeast strain displaying XYNII on the cell surface. These results indicate that xylan is sequentially hydrolyzed to xylose by the codisplayed XYNII and XylA. In a further step toward achieving the simultaneous saccharification and fermentation of xylan, a xylan-utilizing S. cerevisiae strain was constructed by codisplaying XYNII and XylA and introducing genes for xylose utilization, namely, those encoding xylose reductase and xylitol dehydrogenase from Pichia stipitis and xylulokinase from S. cerevisiae. After 62 h of fermentation, 7.1 g of ethanol per liter was directly produced from birchwood xylan, and the yield in terms of grams of ethanol per gram of carbohydrate consumed was 0.30 g/g. These results demonstrate that the direct conversion of xylan to ethanol is accomplished by the xylan-utilizing S. cerevisiae strain.     

High expression of XYL2 coding for xylitol dehydrogenase is necessary for efficient xylose fermentation by engineered Saccharomyces cerevisiae

The traditional ethanologenic yeast Saccharomyces cerevisiae cannot metabolize xylose, which is an abundant sugar in non-crop plants. Engineering this yeast for a practicable fermentation of xylose will therefore improve the economics of bioconversion for the production of fuels and chemicals such as ethanol. One of the most widely employed strategies is to express XYL1, XYL2, and XYL3 genes derived from Scheffersomyces stipitis (formerly Pichia stiptis) in S. cerevisiae. However, the resulting engineered strains have been reported to exhibit large variations in xylitol accumulation and ethanol yields, generating many hypotheses and arguments for elucidating these phenomena. Here we demonstrate that low expression levels of the XYL2 gene, coding for xylitol dehydrogenase (XDH), is a major bottleneck in efficient xylose fermentation. Through an inverse metabolic engineering approach using a genomic library of S. cerevisiae, XYL2 was identified as an overexpression target for improving xylose metabolism. Specifically, we performed serial subculture experiments after transforming a genomic library of wild type S. cerevisiae into an engineered strain harboring integrated copies of XYL1, XYL2 and XYL3. Interestingly, the isolated plasmids from efficient xylose-fermenting transformants contained XYL2. This suggests that the integrated XYL2 migrated into a multi-copy plasmid through homologous recombination. It was also found that additional overexpression of XYL2 under the control of strong constitutive promoters in a xylose-fermenting strain not only reduced xylitol accumulation, but also increased ethanol yields. As the expression levels of XYL2 increased, the ethanol yields gradually improved from 0.1 to 0.3g ethanol/g xylose, while the xylitol yields significantly decreased from 0.4 to 0.1g xylitol/g xylose. These results suggest that strong expression of XYL2 is a necessary condition for developing efficient xylose-fermenting strains.     

A modified Saccharomyces cerevisiae strain that consumes L-Arabinose and produces ethanol

Metabolic engineering is a powerful method to improve, redirect, or generate new metabolic reactions or whole pathways in microorganisms. Here we describe the engineering of a Saccharomyces cerevisiae strain able to utilize the pentose sugar L-arabinose for growth and to ferment it to ethanol. Expanding the substrate fermentation range of S. cerevisiae to include pentoses is important for the utilization of this yeast in economically feasible biomass-to-ethanol fermentation processes. After overexpression of a bacterial L-arabinose utilization pathway consisting of Bacillus subtilis AraA and Escherichia coli AraB and AraD and simultaneous overexpression of the L-arabinose-transporting yeast galactose permease, we were able to select an L-arabinose-utilizing yeast strain by sequential transfer in L-arabinose media. Molecular analysis of this strain, including DNA microarrays, revealed that the crucial prerequisite for efficient utilization of L-arabinose is a lowered activity of L-ribulokinase. Moreover, high L-arabinose uptake rates and enhanced transaldolase activities favor utilization of L-arabinose. With a doubling time of about 7.9 h in a medium with L-arabinose as the sole carbon source, an ethanol production rate of 0.06 to 0.08 g of ethanol per g (dry weight). h(-1) under oxygen-limiting conditions, and high ethanol yields, this yeast strain should be useful for efficient fermentation of hexoses and pentoses in cellulosic biomass hydrolysates.     

A highly efficient single-step,markerless strategy for multi-copy chromosomal integration of large biochemical pathways in Saccharomyces cerevisiae

Despite recent advances in genome editing capabilities for the model organism Saccharomyces cerevisiae, the chromosomal integration of large biochemical pathways for stable industrial production remains challenging. In this work, we developed a simple platform for high-efficiency, single-step, markerless, multi-copy chromosomal integration of full biochemical pathways in Saccharomyces cerevisiae. In this Di-CRISPR (delta integration CRISPR-Cas) platform based on the Clustered Regularly Interspaced Short Palindromic Repeats (CRISPR) and CRISPR-associated systems (Cas), we specifically designed guide RNA sequences to target multiple delta sites in the yeast genome. The generation of double stranded breaks at the delta sites allowed simultaneous integration of multiple copies of linearized donor DNA containing large biochemical pathways. With our newly developed Di-CRISPR platform, we were able to attain highly efficient and markerless integration of large biochemical pathways and achieve an unprecedented 18-copy genomic integration of a 24 kb combined xylose utilization and (R,R)-2,3-butanediol (BDO) production pathway in a single step, thus generating a strain that was able to produce BDO directly from xylose. The simplicity and high efficiency of the Di-CRISPR platform could provide a superior alternative to high copy plasmids and would render this platform an invaluable tool for genome editing and metabolic engineering in S. cerevisiae.     

D-xylose utilization by Saccharomyces cerevisiae

Although it is generally accepted that Saccharomyces cerevisiae is unable to assimilate D-xylose, four strains were found to utilize xylose aerobically at different efficiencies in the presence of a mixture of substrates. The degree of D-xylose utilization by S. cerevisiae ATCC 26602 depended upon the presence of other substrates or yeast extract. The greatest amount of xylose (up to 69% over 7 d) was utilized when sugar substrates such as D-ribose were co-metabolized. Much lower degrees of utilization occurred with co-metabolism of organic acids, polyols or ethanol. A mixture of D-glucose, D-ribose, D-raffinose, glycerol and D-xylose resulted in greater xylose utilization than the presence of a single substrate and xylose. The absence of growth on a co-substrate alone did not prevent the utilization of xylose in its presence. Xylose was co-metabolized with ribose under anaerobic conditions but at a much slower rate than under aerobic conditions. When [14C]xylose was utilized in the presence of ribose under anaerobic conditions, the radioactive label was detected mainly in xylitol and not in the small amounts of ethanol produced. Under aerobic conditions the radioactive label was distributed between xylitol (91.3 +/- 0.8%), CO2 (2.6 +/- 2.3%) and biomass (1.7 +/- 0.6%). No other metabolic products were detected. Whereas most xylose was dissimilated rather than assimilated by S. cerevisiae, the organism apparently possesses a pathway which completely oxidizes xylose in the presence of another substrate.     

Xylose-metabolizing Saccharomyces cerevisiae strains overexpressing the TKL1 and TAL1 genes encoding the pentose phosphate pathway enzymes transketolase and transaldolase.

Saccharomyces cerevisiae was metabolically engineered for xylose utilization. The Pichia stipitis CBS 6054 genes XYL1 and XYL2 encoding xylose reductase and xylitol dehydrogenase were cloned into S. cerevisiae. The gene products catalyze the two initial steps in xylose utilization which S. cerevisiae lacks. In order to increase the flux through the pentose phosphate pathway, the S. cerevisiae TKL1 and TAL1 genes encoding transketolase and transaldolase were overexpressed. A XYL1- and XYL2-containing S. cerevisiae strain overexpressing TAL1 (S104-TAL) showed considerably enhanced growth on xylose compared with a strain containing only XYL1 and XYL2. Overexpression of only TKL1 did not influence growth. The results indicate that the transaldolase level in S. cerevisiae is insufficient for the efficient utilization of pentose phosphate pathway metabolites. Mixtures of xylose and glucose were simultaneously consumed with the recombinant strain S104-TAL. The rate of xylose consumption was higher in the presence of glucose. Xylose was used for growth and xylitol formation, but not for ethanol production. Decreased oxygenation resulted in impaired growth and increased xylitol formation. Fermentation with strain S103-TAL, having a xylose reductase/xylitol dehydrogenase ratio of 0.5:30 compared with 4.2:5.8 for S104-TAL, did not prevent xylitol formation.     

Repeated-batch fermentations of xylose and glucose-xylose mixtures using a respiration-deficient Saccharomyces cerevisiae engineered for xylose metabolism

Xylose-fermenting Saccharomyces strains are needed for commercialization of ethanol production from lignocellulosic biomass. Engineered Saccharomyces cerevisiae strains expressing XYL1, XYL2 and XYL3 from Pichia stipitis, however, utilize xylose in an oxidative manner, which results in significantly lower ethanol yields from xylose as compared to glucose. As such, we hypothesized that reconfiguration of xylose metabolism from oxidative into fermentative manner might lead to efficient ethanol production from xylose. To this end, we generated a respiration-deficient (RD) mutant in order to enforce engineered S. cerevisiae to utilize xylose only through fermentative metabolic routes. Three different repeated-batch fermentations were performed to characterize characteristics of the respiration-deficient mutant. When fermenting glucose as a sole carbon source, the RD mutant exhibited near theoretical ethanol yields (0.46 g g(-1)) during repeated-batch fermentations by recycling the cells. As the repeated-batch fermentation progressed, the volumetric ethanol productivity increased (from 7.5 to 8.3 g L(-1)h(-1)) because of the increased biomass from previous cultures. On the contrary, the mutant showed decreasing volumetric ethanol productivities during the repeated-batch fermentations using xylose as sole carbon source (from 0.4 to 0.3 g L(-1)h(-1)). The mutant did not grow on xylose and lost fermenting ability gradually, indicating that the RD mutant cannot maintain a good fermenting ability on xylose as a sole carbon source. However, the RD mutant was capable of fermenting a mixture of glucose and xylose with stable yields (0.35 g g(-1)) and productivities (0.52 g L(-1)h(-1)) during the repeated-batch fermentation. In addition, ethanol yields from xylose during the mixed sugar fermentation (0.30 g g(-1)) were higher than ethanol yields from xylose as a sole carbon source (0.21 g g(-1)). These results suggest that a strategy for increasing ethanol yield through respiration-deficiency can be applied for the fermentation of lignocellulosic hydrolyzates containing glucose and xylose.     

Synthesis of polyketides from low cost substrates by the thermotolerant yeast Kluyveromyces marxianus

Kluyveromyces marxianus is a promising nonconventional yeast for biobased chemical production due to its rapid growth rate, high TCA cycle flux, and tolerance to low pH and high temperature. Unlike Saccharomyces cerevisiae, K. marxianus grows on low-cost substrates to cell densities that equal or surpass densities in glucose, which can be beneficial for utilization of lignocellulosic biomass (xylose), biofuel production waste (glycerol), and whey (lactose). We have evaluated K. marxianus for the synthesis of polyketides, using triacetic acid lactone (TAL) as the product. The 2-pyrone synthase (2-PS) was expressed on a CEN/ARS plasmid in three different strains, and the effects of temperature, carbon source, and cultivation strategy on TAL levels were determined. The highest titer was obtained in defined 1% xylose medium at 37°C, with substantial titers at 41 and 43°C. The introduction of a high-stability 2-PS mutant and a promoter substitution increased titer four-fold. 2-PS expression from a multi-copy pKD1-based plasmid improved TAL titers a further five-fold. Combining the best plasmid, promoter, and strain resulted in a TAL titer of 1.24 g/L and a yield of 0.0295 mol TAL/mol carbon for this otherwise unengineered strain in 3 ml tube culture. This is an excellent titer and yield (on xylose) before metabolic engineering or fed-batch culture relative to other hosts (on glucose), and demonstrates the promise of this rapidly growing and thermotolerant yeast species for polyketide production.