Exploration of a natural reservoir of flocculating genes from various Saccharomyces cerevisiae strains and improved ethanol fermentation using stable genetically engineered flocculating yeast strains

Flocculating yeast strains with good fermentation ability are desirable for brewing industry as well as for fuel ethanol production, however, the genetic diversity of the flocculating genes from natural yeast strains is largely unexplored. In this study, FLO1, FLO5, FLO9, FLO10 and FLO11 PCR products were obtained from 16 yeast strains from various sources, and the PCR product amplified from FLO1 of the self-flocculating yeast strain SPSC01 was used for the construction of expression cassette flanked by homologous fragments of the endonuclease gene HO for chromosome integration. A genetically engineered flocculating yeast BHL01 with good fermentation performance was obtained by transforming an industrial strain Saccharomyces cerevisiae 4126 with the expression cassette. The fermentation performances of SPSC01 and BHL01 in flask fermentation were compared using 208 g/L glucose. BHL01 completed the fermentation 8 h earlier than SPSC01, while no significant difference between BHL01 and S. cerevisiae 4126 was observed. In very high gravity repeated batch ethanol fermentation using 255 g/L glucose, BHL01 maintained stable flocculation for at least over 24 batches, while SPSC01 displayed severe deflocculation under the same conditions. The natural reservoir of flocculating genes from yeast strains may represent an unexplored gene source for the construction of new flocculating yeast strains for improved ethanol production.     

Ethanol-induced yeast flocculation directed by the promoter of TPS1 encoding trehalose-6-phosphate synthase 1 for efficient ethanol production

Yeast flocculation is an important trait in the brewing industry as well as in ethanol production, through which biomass can be recovered by cost-effective sedimentation. However, mass transfer limitation may affect yeast growth and ethanol fermentation if the flocculation occurs earlier before fermentation is completed. In this article, a novel type of cell-cell flocculation induced by trehalose-6-phosphate synthase 1 (TPS1) promoter was presented. The linear cassette HO-P(TPS1)-FLO1(SPSC01)-KanMX4-HO was constructed to transform the non-flocculating industrial yeast S. cerevisiae 4126 by chromosome integration to obtain a new flocculating yeast strain, ZLH01, whose flocculation was induced by ethanol produced during fermentation. The experimental results illustrated that flocculation of ZLH01 was triggered by 3% (v/v) ethanol and enhanced as ethanol concentration increased till complete flocculation was achieved at ethanol concentration of 8% (v/v). Real time PCR analysis confirmed that the expression of FLO1(SPSC01) was dependent on ethanol concentration. The growth and ethanol fermentation of ZLH01 were improved significantly, compared with the constitutive flocculating yeast BHL01 engineered with the same FLO gene but directed by the constitutive 3-phosphoglycerate kinase promoter PGK1, particularly under high temperature conditions. These characteristics make the engineered yeast more suitable for ethanol production from industrial substrates under high gravity and temperature conditions. In addition, this strategy offers advantage in inducing differential expression of other genes for metabolic engineering applications of S. cerevisiae.     

Construction of flocculent industrial yeast by the yeast flocculation gene <Emphasis Type="Italic">FLO1</Emphasis>

The structure gene FLO1 from Saccharomyces cerevisiae W303-1A encoding a flocculation protein and the G418 resistance gene kanMX from plasmid pUG6 were amplified by PCR method. The expression vector pYX212 harboring FLO1 gene and kanMX gene was transformed into Angel yeast. The transformant Angel yeast F6 was obtained and showed strong and stable flocculation ability during 20 batches inoculation. And the flocculation ability of the transformant Angel yeast F6 showed no difference in the medium with the initial pH ranging from 3.5 to 6.0. Noteworthily, the flocculation onset of the transformant strain was in the early stationary growth phase, not coincident with the glucose depletion in the cultural medium. And in the experiment the ethanol yield and other properties of the transformant Angel yeast F6 were similar to those of the wild-type strain, although its fermentation time was a little slower comparing with the wild-type strain. Those would be potential application for yeast cells to separate and recycle in the fuel ethanol industry.     

Yeast flocculation: New story in fuel ethanol production

Yeast flocculation has been used in the brewing industry to facilitate biomass recovery for a long time, and thus its mechanism of yeast flocculation has been intensively studied. However, the application of flocculating yeast in ethanol production garnered attention mainly in the 1980s and 1990s. In this article, updated research progress in the molecular mechanism of yeast flocculation and the impact of environmental conditions on yeast flocculation are reviewed. Construction of flocculating yeast strains by genetic approach and utilization of yeast flocculation for ethanol production from various feedstocks were presented. The concept of self-immobilized yeast cells through their flocculation is revisited through a case study of continuous ethanol fermentation with the flocculating yeast SPSC01, and their technical and economic advantages are highlighted by comparing with yeast cells immobilized with supporting materials and regular free yeast cells as well. Taking the flocculating yeast SPSC01 as an example, the ethanol tolerance of the flocculating yeast was also discussed.     

Construction of a flocculating yeast for fructose production from inulin

Construction of flocculating yeast lacking for fructose utilisation was realised by integration of the FLO1 flocculation gene in the ribosomal DNA of an hexokinase deficient (hxk1, hxk2) Saccharomyces cerevisiae strain (ATCC36859). Simultaneous production of ethanol and fructose was obtained from glucose/fructose mixtures or from hydrolysed Jerusalem artichoke extracts using the transformed yeast in batch fermentations and in a continuous reactor with internal biomass recycle. This allowed the production of 5 g ethanol/L and 48 g sugars/L containing up to 99 % fructose from diluted hydrolysed Jerusalem artichoke extracts containing 60 g sugars/L. © Rapid Science Ltd. 1998     

Very high gravity ethanol fermentation by flocculating yeast under redox potential-controlled conditions

ABSTRACT: BACKGROUND: Very high gravity (VHG) fermentation using medium in excess of 250 g/L sugars for more than 15 % (v) ethanol can save energy consumption, not only for ethanol distillation, but also for distillage treatment; however, stuck fermentation with prolonged fermentation time and more sugars unfermented is the biggest challenge. Controlling redox potential (ORP) during VHG fermentation benefits biomass accumulation and improvement of yeast cell viability that is affected by osmotic pressure and ethanol inhibition, enhancing ethanol productivity and yield, the most important techno-economic aspect of fuel ethanol production. RESULTS: Batch fermentation was performed under different ORP conditions using the flocculating yeast and media containing glucose of 201 [PLUS-MINUS SIGN] 3.1, 252 [PLUS-MINUS SIGN] 2.9 and 298 [PLUS-MINUS SIGN] 3.8 g/L. Compared with ethanol fermentation by non-flocculating yeast, different ORP profiles were observed with the flocculating yeast due to the morphological change associated with the flocculation of yeast cells. When ORP was controlled at [MINUS SIGN]100 mV, ethanol fermentation with the high gravity (HG) media containing glucose of 201 [PLUS-MINUS SIGN] 3.1 and 252 [PLUS-MINUS SIGN] 2.9 g/L was completed at 32 and 56 h, respectively, producing 93.0 [PLUS-MINUS SIGN] 1.3 and 120.0 [PLUS-MINUS SIGN] 1.8 g/L ethanol, correspondingly. In contrast, there were 24.0 [PLUS-MINUS SIGN] 0.4 and 17.0 [PLUS-MINUS SIGN] 0.3 g/L glucose remained unfermented without ORP control. As high as 131.0 [PLUS-MINUS SIGN] 1.8 g/L ethanol was produced at 72 h when ORP was controlled at [MINUS SIGN]150 mV for the VHG fermentation with medium containing 298 [PLUS-MINUS SIGN] 3.8 g/L glucose, since yeast cell viability was improved more significantly. CONCLUSIONS: No lag phase was observed during ethanol fermentation with the flocculating yeast, and the implementation of ORP control improved ethanol productivity and yield. When ORP was controlled at [MINUS SIGN]150 mV, more reducing power was available for yeast cells to survive, which in turn improved their viability and VHG ethanol fermentation performance. On the other hand, controlling ORP at [MINUS SIGN]100 mV stimulated yeast growth and enhanced ethanol production under the HG conditions. Moreover, the ORP profile detected during ethanol fermentation with the flocculating yeast was less fluctuated, indicating that yeast flocculation could attenuate the ORP fluctuation observed during ethanol fermentation with non-flocculating yeast.     

絮凝选择载体的构建及β葡萄糖苷酶基因在酿酒酵母中的表达

从强絮凝酿酒酵母(Saccharomyces cerevisiae)ABXL-1D菌株中用PCRA-法扩增到絮凝基因(Flocculation gene,FLO1),构建以絮凝基因作选择标记的酿酒酵母表达栽体：用该栽体表达Bacillus polymyxa的β-葡萄糖苷酶基因,转化子可直接从沉淀中筛选。摇瓶培养细胞得到的β-葡萄糖苷酶比活力为3．91u／mg蛋白。在发酵葡萄糖和纤维二糖混合底物时,转化子的葡萄糖残存量明显低于受体菌。这将有利于利用纤维素发酵生产酒精。     

Region of Flo1 Proteins Responsible for Sugar Recognition

Yeast flocculation is a phenomenon which is believed to result from an interaction between a lectin-like protein and a mannose chain located on the yeast cell surface. The FLO1 gene, which encodes a cell wall protein, is considered to play an important role in yeast flocculation, which is inhibited by mannose but not by glucose (mannose-specific flocculation). A new homologue of FLO1, named Lg-FLO1, was isolated from a flocculent bottom-fermenting yeast strain in which flocculation is inhibited by both mannose and glucose (mannose/glucose-specific flocculation). In order to confirm that both FLO1 and Lg-FLO1 are involved in the yeast flocculation phenomenon, the FLO1 gene in the mannose-specific flocculation strain was replaced by the Lg-FLO1 gene. The transformant in which the Lg-FLO1 gene was incorporated showed the same flocculation phenotype as the mannose/glucose-specific flocculation strain, suggesting that the FLO1 and Lg-FLO1 genes encode mannose-specific and mannose/glucose-specific lectin-like proteins, respectively. Moreover, the sugar recognition sites for these sugars were identified by expressing chimeric FLO1 and Lg-FLO1 genes. It was found that the region from amino acid 196 to amino acid 240 of both gene products is important for flocculation phenotypes. Further mutational analysis of this region suggested that Thr-202 in the Lg-Flo1 protein and Trp-228 in the Flo1 protein are involved in sugar recognition.     

絮凝性强的优良面包酵母菌株的选育

通过初筛、单倍体分离、DES诱变、絮凝基因的克隆表达及杂交等育种技术成功构建了高生物量、耐高糖、强絮凝的优良面包酵母菌株(Saccharomyces cerevisiae) ZLTH58(MATa/α,leu,FLO1)。菌株ZLTH58具有双亲的优良性状,遗传性状稳定。对其生物量、耐高糖能力、絮凝特性进行了检测,结果表明,菌株ZLTH58的生物量是原始亲株BL56的1.21倍;耐高糖能力优于原始亲株BL61;絮凝性能明显优于原始亲株BL56和BL61。对其培养条件进行了优化,在优化的培养条件下,生物量可以达到83.06g/L,为初始培养条件下的1.35倍。     

Flocculation gene variability in industrial brewer’s yeast strains

The brewer’s yeast genome encodes a ‘Flo’ flocculin family responsible for flocculation. Controlled floc formation or flocculation at the end of fermentation is of great importance in the brewing industry since it is a cost-effective and environmental-friendly technique to separate yeast cells from the final beer. FLO genes have the notable capacity to evolve and diverge many times faster than other genes. In actual practice, this genetic variability may directly alter the flocculin structure, which in turn may affect the flocculation onset and/or strength in an uncontrolled manner. Here, 16 ale and lager yeast strains from different breweries, one laboratory Saccharomyces cerevisiae and one reference Saccharomyces pastorianus strain, with divergent flocculation strengths, were selected and screened for characteristic FLO gene sequences. Most of the strains could be distinguished by a typical pattern of these FLO gene markers. The FLO1 and FLO10 markers were only present in five out of the 18 yeast strains, while the FLO9 marker was ubiquitous in all the tested strains. Surprisingly, three strongly flocculating ale yeast strains in this screening also share a typical ‘lager’ yeast FLO gene marker. Further analysis revealed that a complete Lg-FLO1 allele was present in these ale yeasts. Taken together, this explicit genetic variation between flocculation genes hampers attempts to understand and control the flocculation behavior in industrial brewer’s yeasts.     

Deletion of tandem repeats causes flocculation phenotype conversion from Flo1 to NewFlo in Saccharomyces cerevisiae

A gene, FLONS, conferring NewFlo-type flocculation ability in yeast was cloned. The 3,396-bp ORF encoded a peptide of 1,132 amino acids with high identity to Flo1 protein. Aligned with the FLO1 gene, two repeated regions (675 and 540 bp) were lost in the middle of FLONS, revealing that this gene was a derived form of the FLO1 gene. The missing repeated sequence contained three highly homologous repeat units. Although the flocculation phenotype of the transformant YTS-S with the FLONS gene was inhibited by both mannose and glucose, it exhibited some distinguished physiological characteristics from the reported typical NewFlo-type flocculation during detailed investigation. The deletion of repeats was suspected to cause conversion of the flocculation phenotype from Flo1 to NewFlo, suggesting that intragenic tandem repeats generated functional variability in Flo1 protein.     

絮凝基因FLO1及FLO1c高表达提高工业酿酒酵母乙酸耐受性及发酵性能

乙酸是生物质乙醇发酵过程中酵母细胞面临的重要抑制剂之一,对细胞生长及发酵性能有强烈的抑制作用。增强酵母菌对乙酸胁迫的耐受性对提高乙醇产率具有重要意义。用分别带有完整絮凝基因FLO1及其重复序列单元C发生缺失的衍生基因FLO1c的重组表达质粒分别转化非絮凝型工业酿酒酵母CE6,获得絮凝型重组酵母菌株6-AF1和6-AF1c。同时以空载体p YCPGA1转化CE6的菌株CE6-V为对照菌株。与CE6-V相比,絮凝酵母明显提高了对乙酸胁迫的耐受性。在0.6%(V/V)乙酸胁迫下,6-AF1和6-AF1c的乙醇产率分别为对照菌株CE6-V的1.56倍和1.62倍;在1.0%(V/V)乙酸胁迫下,6-AF1和6-AF1c的乙醇产率分别为对照菌株CE6-V的1.21倍和1.78倍。可见絮凝能力改造能明显提高工业酿酒酵母的乙酸胁迫耐受性及发酵性能,而且FLO1内重复序列单元C缺失具有更加明显的效果。     

Construction of a flocculating yeast for fuel ethanol production

The expression vector pYX212 harboring FLO1 gene and kanMX gene was transformed into Saccharomyces. cerevisiae ZWA46. The transformant, ZWA46-F2, showed strong and stable flocculation ability during 20 serial batch cultivations. The flocculation onset of the strain is in the early stationary growth phase, not coincident with the glucose depletion in the culture medium. The flocculation ability of the transformant showed no difference with the initial pH ranging from 3.5 to 6.0. Furthermore, the ethanol concentration and other properties of the transformant strain ZWA46-F2 were similar to those of the wild-type strain ZWA46.     

Flocculating Zymomonas mobilis is a promising host to be engineered for fuel ethanol production from lignocellulosic biomass

Whereas Saccharomyces cerevisiae uses the Embden‐Meyerhof‐Parnas pathway to metabolize glucose, Zymomonas mobilis uses the Entner‐Doudoroff (ED) pathway. Employing the ED pathway, 50% less ATP is produced, which could lead to less biomass being accumulated during fermentation and an improved yield of ethanol. Moreover, Z. mobilis cells, which have a high specific surface area, consume glucose faster than S. cerevisiae, which could improve ethanol productivity. We performed ethanol fermentations using these two species under comparable conditions to validate these speculations. Increases of 3.5 and 3.3% in ethanol yield, and 58.1 and 77.8% in ethanol productivity, were observed in ethanol fermentations using Z. mobilis ZM4 in media containing ～100 and 200 g/L glucose, respectively. Furthermore, ethanol fermentation bythe flocculating Z. mobilis ZM401 was explored. Although no significant difference was observed in ethanol yield and productivity, the flocculation of the bacterial species enabled biomass recovery by cost‐effective sedimentation, instead of centrifugation with intensive capital investment and energy consumption. In addition, tolerance to inhibitory byproducts released during biomass pretreatment, particularly acetic acid and vanillin, was improved. These experimental results indicate that Z. mobilis, particularly its flocculating strain, is superior to S. cerevisiae as a host to be engineered for fuel ethanol production from lignocellulosic biomass.     

Kinetics of the selective fermentation of glucose from glucose/fructose mixtures using Saccharomyces cerevisiae ATCC 36859

The kinetics of batch fermentation during the growth of S. cerevisiae ATCC 36859 was studied in various glucose/fructose mixtures. It was found that the growth is inhibited equally by glucose and fructose even though fructose is not consumed to any large extent by the yeast under the conditions tested here. The inhibition of growth by the substrate and ethanol is represented by linear equations. These equations were combined with the MONOD expression in order to formulate equations for the biomass growth, glucose and fructose consumption and ethanol production. Parameter estimates were obtained by fitting these equations to batch fermentation data and so developing models which indicate that the growth is completely inhibited when 62 g/l ethanol is produced by the yeast, while glucose consumption and ethanol production continue up to an ethanol concentration of 152 g/l. Products containing a high concentration of fructose are best produced by using a high initial biomass concentration.     

Breeding of flocculent industrial alcohol yeast strains by self-cloning of the flocculation gene FLO1 and repeated-batch fermentation by transformants

A nonflocculent industrial polyploid yeast strain, Saccharomyces cerevisiae 396-9-6V, was converted to a flocculent one by introducing a functional FLO1 gene at the URA3 locus. The flocculent strain FSC27 obtained was a so-called self-cloned strain, having no bacterial DNA. FSC27 cells could be easily recovered for reuse from fermentation mash without any physical energy. The strain produced a concentration of alcohol as high as 396-9-6V, although the fermentation rate of FSC27 was slightly lower than that of 396-9-6V. When uracil was added to the medium or when URA3 was reintroduced into FSC27 (named FSCU-L18), the fermentation rate and the growth rate increased, and the ethanol concentration produced was higher than that produced by the parent strain. The stable flocculation and high ethanol productivity were observed by using FSCU-L18 during 10 cycles of repeated-batch fermentation test.     

无载体固定化酵母细胞木薯淀粉质原料酒精连续发酵研究

以木薯粉糖化液为发酵底物,在总发酵体积(有效)为15L的悬浮床生物反应器中,对一株粟酒裂殖酵母变异株进行一级和二级连续发酵研究。结果表明,二级连续发酵系统可明显改善一级系统的不足,并取得了平均流加糖液浓度150g/L,发酵强度为97g/L.h,流出液酒精浓度727g/L,残糖浓度374g./L,总糖利用率达90%的较好结果;整个系统在连续一个月的运行中从未发现染菌现象,发酵操作稳定。