Characterization of the impact of acetate and lactate on ethanolic fermentation by Thermoanaerobacter ethanolicus

Ethanolic fermentation of simple sugars is an important step in the production of bioethanol as a renewable fuel. Significant levels of organic acids, which are generally considered inhibitory to microbial metabolism, could be accumulated during ethanolic fermentation, either as a fermentation product or as a by-product generated from pre-treatment steps. To study the impact of elevated concentrations of organic acids on ethanol production, varying levels of exogenous acetate or lactate were added into cultures of Thermoanaerobacter ethanolicus strain 39E with glucose, xylose or cellobiose as the sole fermentation substrate. Our results found that lactate was in general inhibitory to ethanolic fermentation by strain 39E. However, the addition of acetate showed an unexpected stimulatory effect on ethanolic fermentation of sugars by strain 39E, enhancing ethanol production by up to 394%. Similar stimulatory effects of acetate were also evident in two other ethanologens tested, T. ethanolicus X514, and Clostridium thermocellum ATCC 27405, suggesting the potentially broad occurrence of acetate stimulation of ethanolic fermentation. Analysis of fermentation end product profiles further indicated that the uptake of exogenous acetate as a carbon source might contribute to the improved ethanol yield when 0.1% (w/v) yeast extract was added as a nutrient supplement. In contrast, when yeast extract was omitted, increases in sugar utilization appeared to be the likely cause of higher ethanol yields, suggesting that the characteristics of acetate stimulation were growth condition-dependent. Further understanding of the physiological and metabolic basis of the acetate stimulation effect is warranted for its potential application in improving bioethanol fermentation processes.     

Correlation of genomic and physiological traits of thermoanaerobacter species with biofuel yields

Thermophilic anaerobic noncellulolytic Thermoanaerobacter species are of great biotechnological importance in cellulosic ethanol production due to their ability to produce high ethanol yields by simultaneous fermentation of hexose and pentose. Understanding the genome structure of these species is critical to improving and implementing these bacteria for possible biotechnological use in consolidated bioprocessing schemes (CBP) for cellulosic ethanol production. Here we describe a comparative genome analysis of two ethanologenic bacteria, Thermoanaerobacter sp. X514 and Thermoanaerobacter pseudethanolicus 39E. Compared to 39E, X514 has several unique key characteristics important to cellulosic biotechnology, including additional alcohol dehydrogenases and xylose transporters, modifications to pentose metabolism, and a complete vitamin B₁₂ biosynthesis pathway. Experimental results from growth, metabolic flux, and microarray gene expression analyses support genome sequencing-based predictions which help to explain the distinct differences in ethanol production between these strains. The availability of whole-genome sequence and comparative genomic analyses will aid in engineering and optimizing Thermoanaerobacter strains for viable CBP strategies.     

Continuous Cellulosic Bioethanol Fermentation by Cyclic Fed-Batch Cocultivation

Cocultivation of cellulolytic and saccharolytic microbial populations is a promising strategy to improve bioethanol production from the fermentation of recalcitrant cellulosic materials. Earlier studies have demonstrated the effectiveness of cocultivation in enhancing ethanolic fermentation of cellulose in batch fermentation. To further enhance process efficiency, a semicontinuous cyclic fed-batch fermentor configuration was evaluated for its potential in enhancing the efficiency of cellulose fermentation using cocultivation. Cocultures of cellulolytic Clostridium thermocellum LQRI and saccharolytic Thermoanaerobacter pseudethanolicus strain X514 were tested in the semicontinuous fermentor as a model system. Initial cellulose concentration and pH were identified as the key process parameters controlling cellulose fermentation performance in the fixed-volume cyclic fed-batch coculture system. At an initial cellulose concentration of 40 g liter⁻¹, the concentration of ethanol produced with pH control was 4.5-fold higher than that without pH control. It was also found that efficient cellulosic bioethanol production by cocultivation was sustained in the semicontinuous configuration, with bioethanol production reaching 474 mM in 96 h with an initial cellulose concentration of 80 g liter⁻¹ and pH controlled at 6.5 to 6.8. These results suggested the advantages of the cyclic fed-batch process for cellulosic bioethanol fermentation by the cocultures.     

Repeated-batch fermentation of lignocellulosic hydrolysate to ethanol using a hybrid Saccharomyces cerevisiae strain metabolically engineered for tolerance to acetic and formic acids

A major challenge associated with the fermentation of lignocellulose-derived hydrolysates is improved ethanol production in the presence of fermentation inhibitors, such as acetic and formic acids. Enhancement of transaldolase (TAL) and formate dehydrogenase (FDH) activities through metabolic engineering successfully conferred resistance to weak acids in a recombinant xylose-fermenting Saccharomyces cerevisiae strain. Moreover, hybridization of the metabolically engineered yeast strain improved ethanol production from xylose in the presence of both 30 mM acetate and 20 mM formate. Batch fermentation of lignocellulosic hydrolysate containing a mixture of glucose, fructose and xylose as carbon sources, as well as the fermentation inhibitors, acetate and formate, was performed for five cycles without any loss of fermentation capacity. Long-term stability of ethanol production in the fermentation phase was not only attributed to the coexpression of TAL and FDH genes, but also the hybridization of haploid strains.     

An effective and simplified pH-stat control strategy for the industrial fermentation of vitamin B12 by Pseudomonas denitrificans

In order to improve the productivity of vitamin B(12) by Pseudomonas denitrificans carried out in a 120-m(3) fermenter, the effect of pH on vitamin B(12) biosynthesis was investigated. Results obtained from shake flask experiments showed that the feeding of carbon source (beet molasses or glucose) and methyl-group donor (betaine or choline chloride) significantly influenced the pH and the biosynthesis of vitamin B(12). In contrast to beet molasses or choline chloride, using glucose as a feed medium and betaine as a methyl-group donor, pH could be maintained at a stable range. As a result, higher vitamin B(12) production was achieved. Accordingly, an effective and simplified pH-stat control strategy was established for the fermentation of vitamin B(12) in a 120-m(3) industrial fermenter. When the new pH control strategy was applied, pH was stably kept in the range of 7.15-7.30 during fermentation. Thus, 214.3 mug/mL of vitamin B(12) was achieved.     

脱氮假单胞菌生产维生素B12过程中粪卟啉Ⅲ的测定及发酵调控

脱氮假单胞菌发酵生产维生素B₁₂过程中,副产物粪卟啉Ⅲ的积累对产物的代谢合成和分离提取有很大的影响。建立了发酵液中粪卟啉Ⅲ的HPLC快速测定方法,发酵液处理后直接进样测定,检测线性范围为12~275 μg/ml,重复性好。研究了不同供氧水平、二氧化碳浓度和pH值对发酵过程中维生素B₁₂和粪卟啉Ⅲ代谢合成的影响,并在120吨发酵罐中进行了发酵过程优化控制。结果表明:在发酵过程产物的合成期控制适当的供氧水平、控制二氧化碳浓度在8.6±0.8%、维持pH值在7.0±0.12能明显抑制卟啉Ⅲ的生物合成,同时使维生素B₁₂产量提高15%。     

A simple and effective set of PCR-based molecular markers for the monitoring of the Saccharomyces cerevisiae cell population during bioethanol fermentation

One of the defining features of the fermentation process used in the production of bioethanol from sugarcane feedstock is the dynamic nature of the yeast population. Minisatellite molecular markers are particularly useful for monitoring yeast communities because they produce polymorphic PCR products that typically display wide size variations. We compared the coding sequences derived from the genome of the sugarcane bioethanol strain JAY270/PE-2 to those of the reference Saccharomyces cerevisiae laboratory strain S288c, and searched for genes containing insertion or deletion polymorphisms larger than 24 bp. We then designed oligonucleotide primers flanking nine of these sites, and used them to amplify differentially sized PCR products. We analyzed the banding patterns in the most widely adopted sugarcane bioethanol strains and in several indigenous yeast contaminants, and found that our marker set had very good discriminatory power. Subsequently, these markers were used to successfully monitor the yeast cell populations in six sugarcane bioethanol distilleries. Additionally, we showed that most of the markers described here are also polymorphic among strains unrelated to bioethanol production, suggesting that they may be applied universally in S. cerevisiae. Because the relatively large polymorphisms are detectable in conventional agarose gels, our method is well suited to modestly equipped on-site laboratories at bioethanol distilleries, therefore providing both cost and time savings.     

Effect of nutrient limitation and two-stage continuous fermentor design on productivities during "Clostridium ragsdalei" syngas fermentation

The effect of three limiting nutrients, calcium pantothenate, vitamin B₁₂ and cobalt chloride (CoCl₂), on syngas fermentation using “Clostridium ragsdalei” was determined using serum bottle fermentation studies. Significant results from the bottle studies were translated into single- and two-stage continuous fermentor designs. Studies indicated that three-way interactions between the three limiting nutrients, and two-way interactions between vitamin B₁₂ and CoCl₂ had a significant positive effect on ethanol and acetic acid formation. In general, ethanol and acetic acid production ceased at the end of 9 days corresponding to the production of 2.01 and 1.95 g L⁻¹ for the above interactions. Reactor studies indicated the three-way nutrient limitation in two-stage fermentor showed improved acetic acid (17.51 g g⁻¹ cells) and ethanol (14.74 g g⁻¹ cells) yield compared to treatments in single-stage fermentors. These results further support the hypothesis that it is possible to modulate the product formation by limiting key nutrients during C. ragsdalei syngas fermentation.     

盐水球菌Salinicoccus ventosaetal B2-3-5的代谢产物分析及其抑制酪氨酸酶活性的机制

[背景] 酪氨酸酶是黑色素合成过程中的关键酶,也是引起人体色素障碍性疾病和产生果蔬酶促褐变的主要原因。目前,酪氨酸酶抑制剂的开发已引起广泛关注,但一些酪氨酸酶抑制剂如熊果苷、曲酸等均存在一定的安全隐患。微生物资源丰富且具有许多优点,从微生物中寻找特异性强、高效的酪氨酸酶抑制剂已成为该领域研究的热点。[目的] 通过测定分离自新疆乌鲁木齐达坂城盐湖的盐水球菌Salinicoccus ventosaetal B2-3-5和B6-1-4代谢物提取物对酪氨酸酶活性的影响,比较2株菌发酵过程中代谢物的差异,了解所筛选菌株B2-3-5抑制酪氨酸酶活性的机制。[方法] 以曲酸为阳性对照分别测定B2-3-5和B6-1-4这2个菌株发酵产生的代谢物提取物对蘑菇酪氨酸酶的抑制活性;应用LC-MS代谢组学方法检测2株菌在相同条件下产生的所有代谢物质;采用单变量、多元变量、正交偏最小二乘判别分析（Orthogonal Partial Least Squares-Discrimination Analysis,OPLS-DA）法识别差异代谢物;利用层次聚类分析（Hierarchial Cluster Analysis,HCA）法对识别的差异物进行聚类分析;通过Kyoto Encyclopedia of Genes and Genomes （KEGG）代谢通路对比法分析这些差异代谢物主要参与的代谢途径。[结果] 菌株B2-3-5代谢物提取物对蘑菇酪氨酸酶二酚酶活性的抑制率为67%,其IC₅₀为0.277 mg/mL,同属菌株B6-1-4代谢物提取物则对酪氨酸酶无抑制活性。采用代谢组学的检测方法从2株菌的代谢物中筛选出63个差异代谢物,其中氨基酸类化合物、维生素类化合物和羧酸类化合物的种类及相对含量均是B2-3-5菌株明显高于B6-1-4菌株。通过代谢途径分析发现这些差异代谢物主要参与15个代谢通路,其中维生素B6生物合成通路的影响较为显著。[结论] 推测B2-3-5菌株可能是通过增加一些氨基酸类、维生素类及羧酸类等小分子化合物的含量来抑制酪氨酸酶活性。维生素B6代谢途径的上调也表明菌体细胞可通过产生维生素B6与酪氨酸酶中的必需氨基作用或清除酶催化循环过程中产生的活性氧自由基（reactive oxygen species,ROS）来抑制酪氨酸酶活性。     

Genotypic and phenotypic characterization of industrial autochthonous Saccharomyces cerevisiae for the selection of well-adapted bioethanol-producing strains

In northwestern Argentina, sugarcane-derived industrial fermentation is being extensively used for bioethanol production, where highly adaptive native strains compete with the baker's yeast Saccharomyces cerevisiae traditionally used as starter culture. Yeast populations of 10 distilleries from Tucumán (Argentina) were genotypic and phenotypic characterized to select well-adapted bioethanol-producing autochthonous strains to be used as starter cultures for the industrial production of bioethanol fuel. From the 192 isolates, 69.8% were identified as S. cerevisiae, 25.5% as non-Saccharomyces, and 4.7% as Saccharomyces sp. wild yeasts. The majority of S. cerevisiae isolates (68.5%) were non-flocculating yeasts, while the flocculating strains were all obtained from the only continuous fermentation process included in the study. Simple Sequence Repeat analysis revealed a high genetic diversity among S. cerevisiae genotypes, where all of them were very different from the original baker's strain used as starter. Among these, 38 strains multi-tolerant to stress by ethanol (8%), temperature (42.5 °C) and pH (2.0) were obtained. No major differences were found among these strains in terms of ethanol production and residual sugars in batch fermentation experiments with cell recycling. However, only 10 autochthonous strains maintained their viability (more than 80%) throughout five consecutive cycles of sugarcane-based fermentations. In summary, 10 autochthonous isolates were found to be superior to baker's yeast used as starter culture (S. cerevisiae Calsa) in terms of optimal technological, physiological and ecological properties. The knowledge generated on the indigenous yeast populations in industrial fermentation processes of bioethanol-producing distilleries allowed the selection of well-adapted bioethanol-producing strains.     

Highly efficient bioethanol production by a Saccharomyces cerevisiae strain with multiple stress tolerance to high temperature, acid and ethanol

Use of super strains exhibiting tolerance to high temperature, acidity and ethanol is a promising way to make ethanol production economically feasible. We describe here the breeding and performance of such a multiple-tolerant strain of Saccharomyces cerevisiae generated by a spore-to-cell hybridization technique without recombinant DNA technology. A heterothallic strain showing a high-temperature (41°C) tolerant (Htg(+)) phenotype, a derivative from a strain isolated from nature, was crossed with a homothallic strain displaying high-ethanol productivity (Hep(+)), a stock culture at the Thailand Institute of Scientific and Technological Research. The resultant hybrid TJ14 displayed ability to rapidly utilize glucose, and produced ethanol (46.6g/l) from 10% glucose fermentation medium at high temperature (41°C). Not only ethanol productivity at 41°C but also acid tolerance (Acd(+)) was improved in TJ14 as compared with its parental strains, enabling TJ14 to grow in liquid medium even at pH 3. TJ14 maintained high ethanol productivity (46.0g/l) from 10% glucose when fermentation was done under multiple-stress conditions (41°C and pH 3.5). Furthermore, when TJ14 was subjected to a repeated-batch fermentation scheme, the growth and ethanol production of TJ14 were maintained at excellent levels over ten cycles of fermentation. Thus, the multiple-stress (Htg(+) Hep(+) Acd(+)) resistant strain TJ14 should be useful for cost-effective bioethanol production under high-temperature and acidic conditions.     

Comparison of SHF and SSF processes from steam-exploded wheat straw for ethanol production by xylose-fermenting and robust glucose-fermenting Saccharomyces cerevisiae strains

In this study, bioethanol production from steam-exploded wheat straw using different process configurations was evaluated using two Saccharomyces cerevisiae strains, F12 and Red Star. The strain F12 has been engineerically modified to allow xylose consumption as cereal straw contain considerable amounts of pentoses. Red Star is a robust hexose-fermenting strain used for industrial fuel ethanol fermentations and it was used for comparative purposes. The highest ethanol concentration, 23.7 g/L, was reached using the whole slurry (10%, w/v) and the recombinant strain (F12) in an SSF process, it showed an ethanol yield on consumed sugars of 0.43 g/g and a volumetric ethanol productivity of 0.7 g/L h for the first 3 h. Ethanol concentrations obtained in SSF processes were in all cases higher than those from SHF at the same conditions. Furthermore, using the whole slurry, final ethanol concentration was improved in all tests due to the increase of potential fermentable sugars in the fermentation broth. Inhibitory compounds present in the pretreated wheat straw caused a significantly negative effect on the fermentation rate. However, it was found that the inhibitors furfural and HMF were completely metabolized by the yeast during SSF by metabolic redox reactions. An often encountered problem during xylose fermentation is considerable xylitol production that occurs due to metabolic redox imbalance. However, in our work this redox imbalance was counteracted by the detoxification reactions and no xylitol was produced.     

A strategy to prevent the occurrence of Lactobacillus strains using lactate-tolerant yeast Candida glabrata in bioethanol production

Contamination of Lactobacillus sp. in the fermentation broth of bioethanol production decreases ethanol production efficiency. Although the addition of lactate to the broth can effectively inhibit the growth of Lactobacillus sp., it also greatly reduces the fermentation ability of Saccharomyces cerevisiae. To overcome this conflict, lactate-tolerant yeast strains were screened. Candida glabrata strain NFRI 3164 was found to exhibit both higher levels of lactate tolerance and fermentation ability. Co-cultivation of C. glabrata was performed with Lactobacillus brevis and Lb. fermentum, which were reported as major contaminating bacteria during bioethanol production, in culture medium containing 2% lactate. Under these culture conditions, the growth of Lactobacillus strains was greatly inhibited, but the ethanol production of C. glabrata was not significantly affected. Our data show the possibility of designing an effective fuel ethanol production process that eliminates contamination by Lactobacillus strains through the combined use of lactate addition and C. glabrata.     

Simultaneous saccharification and fermentation of steam-pretreated bagasse using Saccharomyces cerevisiae TMB3400 and Pichia stipitis CBS6054

Sugarcane bagasse--a residue from sugar and ethanol production from sugar cane--is a potential raw material for lignocellulosic ethanol production. This material is high in xylan content. A prerequisite for bioethanol production from bagasse is therefore that xylose is efficiently fermented to ethanol. In the current study, ethanolic fermentation of steam-pretreated sugarcane bagasse was assessed in a simultaneous saccharification and fermentation (SSF) set-up using either Saccharomyces cerevisiae TMB3400, a recombinant xylose utilizing yeast strain, or Pichia stipitis CBS6054, a naturally xylose utilizing yeast strain. Commercial cellulolytic enzymes were used and the content of water insoluble solids (WIS) was 5% or 7.5%. S. cerevisiae TMB3400 consumed all glucose and large fraction of the xylose in SSF. Almost complete xylose conversion could be achieved at 5% WIS and 32 degrees C. Fermentation did not occur with P. stipitis CBS6054 at pH 5.0. However, at pH 6.0, complete glucose conversion and high xylose conversion (>70%) was obtained. Microaeration was required for P. stipitis CBS6054. This was not necessary for S. cerevisiae TMB3400.     

Hydrogen production by immobilized R. faecalis RLD-53 using soluble metabolites from ethanol fermentation bacteria E. harbinense B49

In order to increase the hydrogen yield from glucose, hydrogen production by immobilized Rhodopseudomonas faecalis RLD-53 using soluble metabolites from ethanol fermentation bacteria Ethanoligenens harbinense B49 was investigated. The soluble metabolites from dark-fermentation mainly were ethanol and acetate, which could be further utilized for photo-hydrogen production. Hydrogen production by B49 was noticeably affected by the glucose and phosphate buffer concentration. The maximum hydrogen yield (1.83 mol H₂/mol glucose) was obtained at 9 g/l glucose. In addition, we found that the ratio of acetate/ethanol (A/E) increased with increasing phosphate buffer concentration, which is favorable to further photo-hydrogen production. The total hydrogen yield during dark- and photo-fermentation reached its maximum value (6.32 mol H₂/mol glucose) using 9 g/l glucose, 30 mmol/l phosphate buffers and immobilized R. faecalis RLD-53. Results demonstrated that the combination of dark- and photo- fermentation was an effective and efficient process to improve hydrogen yield from a single substrate.     

不同信号肽对酿酒酵母蔗糖转化酶Suc2分泌表达水平的影响

目前，绝大多数酿酒酵母（Saccharomyces cerevisiae）菌株利用菊糖生产乙醇的能力有限，而蔗糖转化酶Suc2是酿酒酵母水解菊糖的关键酶，其分泌水平直接影响酿酒酵母转化菊糖为乙醇的性能。为提高酿酒酵母中蔗糖转化酶Suc2的分泌表达水平，利用生物信息学的分析方法选择出11种不同的分泌信号肽，包括酿酒酵母内源性、其他菌株来源以及已报道序列优化改造的信号肽，将它们融合至Suc2并构建了相应的酿酒酵母BY4741重组菌。其中，酿酒酵母内源分泌信号肽AGA2能使蔗糖转化酶Suc2更有效的分泌，含有信号肽AGA2的重组菌BY-AG的蔗糖酶酶活和菊糖酶酶活相对于含有天然信号肽的原始菌BY-S分别提高42%和26%，其利用菊糖产乙醇能力较原始菌提高了32%，乙醇产量达到78.11 g/L。在使用毕赤酵母（Pichia pastoris）分泌信号肽MSB2时，蔗糖转化酶Suc2的分泌水平也有提高，含有信号肽MSB2的重组菌BY-MS较原始菌BY-S的蔗糖酶酶活和菊糖酶酶活分别提高了80%和74%，同时，利用菊糖产乙醇能力也提高了56%，产量达到86.31 g/L。最后，对重组菌BY-MS摇瓶发酵过程中的生物量、蔗糖酶酶活、残糖总量和乙醇产量进行了监测，结果表明，重组菌BY-MS的发酵性能较原始菌BY-S有显著提高。本研究为提高蔗糖转化酶Suc2的分泌水平、构建高效菊糖基乙醇生产菌株提供参考。     

液泡蛋白酶B对酿酒酵母高温乙醇发酵效率的影响

【目的】提高酿酒酵母的高耐温性,从而提高菌株在高温下的乙醇发酵性能。【方法】利用染色体整合过表达酿酒酵母液泡蛋白酶B编码基因PRB1。【结果】在41 °C高温条件下进行乙醇发酵,过表达PRB1基因的重组酿酒酵母菌株可在31 h内消耗全部的葡萄糖,而对照菌株在相同时间内仅消耗不到一半的葡萄糖。【结论】利用蛋白酶B基因过表达可构建耐高温酿酒酵母菌株,提高在高温条件下乙醇的发酵效率。     

Fermentation performance of engineered and evolved xylose-fermenting Saccharomyces cerevisiae strains

Lignocellulose hydrolysate is an abundant substrate for bioethanol production. The ideal microorganism for such a fermentation process should combine rapid and efficient conversion of the available carbon sources to ethanol with high tolerance to ethanol and to inhibitory components in the hydrolysate. A particular biological problem are the pentoses, which are not naturally metabolized by the main industrial ethanol producer Saccharomyces cerevisiae. Several recombinant, mutated, and evolved xylose fermenting S. cerevisiae strains have been developed recently. We compare here the fermentation performance and robustness of eight recombinant strains and two evolved populations on glucose/xylose mixtures in defined and lignocellulose hydrolysate-containing medium. Generally, the polyploid industrial strains depleted xylose faster and were more resistant to the hydrolysate than the laboratory strains. The industrial strains accumulated, however, up to 30% more xylitol and therefore produced less ethanol than the haploid strains. The three most attractive strains were the mutated and selected, extremely rapid xylose consumer TMB3400, the evolved C5 strain with the highest achieved ethanol titer, and the engineered industrial F12 strain with by far the highest robustness to the lignocellulosic hydrolysate.