Mutants of the pentose‐fermenting yeast Pichia stipitis with improved tolerance to inhibitors in hardwood spent sulfite liquor

Mutants of Pichia stipitis NRRL Y‐7124 able to tolerate and produce ethanol from hardwood spent sulfite liquor (HW SSL) were obtained by UV mutagenesis. P. stipitis cells were subjected to three successive rounds of UV mutagenesis, each followed by screening first on HW SSL gradient plates and then in diluted liquid HW SSL. Six third generation mutants with greater tolerance to HW SSL as compared to the wild type (WT) were isolated. The WT strain could not grow in HW SSL unless it was diluted to 65% (v/v). In contrast, the third generation mutants were able to grow in HW SSL diluted to 75% (v/v). Mutants PS301 and PS302 survived even in 80% (v/v) HW SSL, although there was no increase in cell number. All the third generation mutants exhibited higher growth rates but significantly lower growth yields on xylose or glucose compared to the WT. The mutants fermented 4% (w/v) glucose as efficiently as the WT and fermented 4% (w/v) xylose more efficiently with a higher ethanol yield than the WT. In a medium containing 4% (w/v) each of xylose and glucose, all the third generation mutants utilized glucose as efficiently and xylose more efficiently than the WT. This resulted in higher ethanol yield by the mutants. The mutants retained the ability to utilize galactose and mannose and ferment them to ethanol. Arabinose was consumed slowly by both the mutants and WT with no ethanol production. In 60% (v/v) HW SSL, the mutants utilized and fermented glucose, mannose, galactose and xylose while the WT could not ferment any of these sugars. Biotechnol. Bioeng. 2009; 104: 892–900. © 2009 Wiley Periodicals, Inc.     

Ethanol production from eucalyptus wood hemicellulose hydrolysate by Pichia stipitis

Ethanol production was evaluated from eucalyptus wood hemicellulose acid hydrolysate using Pichia stipitis NRRL Y-7124. An initial lag phase characterized by flocculation and viability loss of the yeast inoculated was observed. Subsequently, cell regrowth occurred with sequential consumption of sugars and production of ethanol. Polyol formation was detected. Acetic acid present in the hydrolysate was an important inhibitor of the fermentation, reducing the rate and the yield. Its toxic effect was due essentially to its undissociated form. The fermentation was more effective at an oxygen transfer rate between 1.2 and 2.4 mmol/L h and an initial pH of 6.5. The hydrolysate used in the experiences had the following composition (expressed in grams per liter): xylose 30, arabinose 2.8, glucose 1.5, galactose 3.7, mannose 1.0, cellobiose 0.5, acetic acid 10, glucuronic acid 1.5, and galacturonic acid 1.0. The best values obtained were maximum ethanol concentration 12.6 g/L, fermentation time 75 h, fermentable sugar consumption 99% ethanol yield 0.35 g/g sugars consumed, and volumetric ethanol productivity 4 g/L day. (c) 1992 John Wiley & Sons, Inc.     

树干毕赤酵母NLP31发酵产乙醇的研究

研究了树干毕赤酵母NLP31在木糖质量浓度为45 g/L的3种发酵培养基Ⅰ、Ⅱ和Ⅲ上发酵3轮的发酵性能以及在45 g/L木糖或混合糖(葡萄糖30 g/L,木糖15 g/L)的发酵培养基Ⅲ上的代谢历程。结果表明:树干毕赤酵母NLP31在发酵培养基Ⅲ上,乙醇浓度和乙醇得率均达到最高,分别为(17.29±0.15)g/L和(84.65±0.58)%。在45 g/L木糖或混合糖(葡萄糖30 g/L,木糖15 g/L)的发酵培养基Ⅲ上的代谢历程表明:混合糖发酵达到最大乙醇得率的时间仅为12 h,要比单一木糖发酵缩短了8 h。树干毕赤酵母NLP31在以廉价的无机N源为发酵培养基上的乙醇发酵性能高,能够降低燃料乙醇的生产成本。     

树干毕赤酵母和酿酒酵母混合糖发酵产乙醇

以树干毕赤酵母和酿酒酵母为发酵菌株,酸性蒸汽爆破玉米秸秆预水解液和纯糖模拟液为C源,采用固定化酵母细胞的方法,研究了酸爆玉米秸秆预水解液初始pH、N源种类及其浓度、3种发酵模式对树干毕赤酵母戊糖发酵的影响。结果表明:玉米秸秆预水解液适合发酵的初始pH范围为6.0～7.0;1.0 g/L的(NH4)2SO4作为N源,在40 g/L葡萄糖和25 g/L木糖培养基中发酵24 h,糖利用率达到99.47%,乙醇质量浓度为24.72 g/L,优于尿素和蛋白胨作为N源;3种模式的发酵体系中,以游离树干毕赤酵母和固定化酿酒酵母发酵性能最好,糖利用率和乙醇得率分别为99.43%和96.39%。     

Ethanol production from spent cherry brine

Spent cherry brine is an acidic byproduct of maraschino cherry processing and typically consists of variable amounts of glucose and fructose of up to 11% fermentable solids, 0.5–1.5% CaCl₂, up to 0.4% sulfur dioxide, sorbitol, and lesser amounts of other cherry constituents. Disposal of brine represents a significant cost to processors because of its high biological oxygen demand. As an alternative, brine was tested as a substrate for ethanol production. Initially, the toxic level of sulfur dioxide was reduced by raising brine pH to 8.0 to precipitate calcium sulfite. Because alkalinization was subsequently found to result in a 10-fold reduction in phosphorous, brines were titrated with phosphoric acid to pH 6.0 prior to inoculation with Saccharomyces cerevisiae. All strains of Saccharomyces cerevisiae tested were able to ferment all lots of Ca(OH)₂-treated and phosphorous-enriched brines efficiently. One lot of brine containing 10% (w/v) fermentable sugar yielded 4.7% (w/v) ethanol in 4 days. Received 24 December 1996/ Accepted in revised form 14 April 1997     

Identification of white-rot and soft-rot fungi increasing ethanol production from spent sulfite liquor in co-culture with Saccharomyces cerevisiae

Aim:  To identify fungi that are capable of increasing ethanol production from lignocellulose in spent sulfite liquor.
Methods and Results:  In a batch fermentation study, the fungal mix could produce 24·61 g l⁻¹ ethanol using spent sulfite liquor as substrate. The fungal mix grew well on glucose, xylose, hemicellulose and cellulose. In addition, we were able to identify the fungal mix by use of PCR-amplification of DNA and sequencing, and they were identified as Chalara parvispora and Trametes hirsuta/T. versicolor. In a reconstitution study, the identified fungi were shown to produce equal amount of ethanol as the fungal mix. We were also able to show that C. parvispora could produce ethanol from xylose.
Conclusion:  The present study has shown that ethanol production from biomass can be increased by use of C. parvispora and T. versicolor when compared with fermentation using only S. cerevisiae .
Significance and Impact of the Study:  The study shows that refining biomass by ethanol production from spent sulfite liquor, a lignocellulose material, can be increased by adding C. parvispora and T. versicolor , and it is thus of great potential economical impact.     

树干毕赤酵母木糖还原酶基因的克隆及在大肠杆菌中的表达

根据NCBI中的木糖还原酶基因序列设计引物,利用高保真聚合酶克隆树干毕赤酵母木糖还原酶基因,加A后克隆到质粒pGM-T中,测序验证.然后将目的基因克隆到舍有强启动子的穿梭表达载体p424GPD中,构建含有XYL1基因的重组质粒p424GPD-XYL1.将p424GPD-XYL1转化到大肠杆菌中,提取总蛋白,聚丙烯酰胺凝胶电泳分析.酶活测定确定木糖还原酶基因XYL1在大肠杆菌中得到活性表达,表明表达载体构建成功.表达载体的成功构建为后续构建重组酿酒酵母利用木糖发酵奠定基础.     

酚酮类对树干毕赤酵母乙醇发酵及脂肪酸组成的影响

木质素降解产物对微生物产生的抑制作用,是燃料乙醇生物炼制的主要瓶颈之一。本文以树干毕赤酵母为发酵菌株,研究木质素降解产物中3种酚酮类(4-羟基苯乙酮、4-羟基-3-甲氧基苯乙酮、4-羟基-3,5-二甲氧基苯乙酮)对其木糖乙醇发酵及酵母细胞脂肪酸组成的影响。采用高效液相色谱(HPLC)和气相色谱-质谱联用(GC/MS)技术对乙醇发酵性能和酵母细胞脂肪酸组成进行分析。研究结果表明,酚酮类物质对乙醇发酵呈现抑制作用且其分子量越低抑制作用越明显,当4-羟基苯乙酮浓度为1.50 g/L时,发酵24 h的木糖利用率、乙醇得率和乙醇浓度分别下降了42.47%、5.30%和9.76 g/L;培养基中存在酚酮类物质时,酵母细胞中的不饱和脂肪酸的比例上升,添加1.50 g/L的3种酚酮类物质后,树干毕赤酵母细胞不饱和脂肪酸和饱和脂肪酸的比例从原来的2.58分别上升到3.03、3.06和3.61,酵母细胞膜的流动性随之上升,不稳定性提高。因此,酚酮类物质能够降低酵母生长、提高不饱和脂肪酸的比例以及降低乙醇发酵能力,有效降低或去除木质素降解产物含量是提高木质纤维原料生物炼制的关键。     

Generation of the improved recombinant xylose-utilizing Saccharomyces cerevisiae TMB 3400 by random mutagenesis and physiological comparison with Pichia stipitis CBS 6054

The recombinant xylose-utilizing Saccharomyces cerevisiae TMB 3399 was constructed by chromosomal integration of the genes encoding D-xylose reductase (XR), xylitol dehydrogenase (XDH), and xylulokinase (XK). S. cerevisiae TMB 3399 was subjected to chemical mutagenesis with ethyl methanesulfonate and, after enrichment, 33 mutants were selected for improved growth on D-xylose and carbon dioxide formation in Durham tubes. The best-performing mutant was called S. cerevisiae TMB 3400. The novel, recombinant S. cerevisiae strains were compared with Pichia stipitis CBS 6054 through cultivation under aerobic, oxygen-limited, and anaerobic conditions in a defined mineral medium using only D-xylose as carbon and energy source. The mutation led to a more than five-fold increase in maximum specific growth rate, from 0.0255 h(-1) for S. cerevisiae TMB 3399 to 0.14 h(-1) for S. cerevisiae TMB 3400, whereas P. stipitis grew at a maximum specific growth rate of 0.44 h(-1). All yeast strains formed ethanol only under oxygen-limited and anaerobic conditions. The ethanol yields and maximum specific ethanol productivities during oxygen limitation were 0.21, 0.25, and 0.30 g ethanol g xylose(-1) and 0.001, 0.10, and 0.16 g ethanol g biomass(-1) h(-1) for S. cerevisiae TMB 3399, TMB 3400, and P. stipitis CBS 6054, respectively. The xylitol yield under oxygen-limited and anaerobic conditions was two-fold higher for S. cerevisiae TMB 3399 than for TMB 3400, but the glycerol yield was higher for TMB 3400. The specific activity, in U mg protein(-1), was higher for XDH than for XR in both S. cerevisiae TMB 3399 and TMB 3400, while P. stipitis CBS 6054 showed the opposite relation. S. cerevisiae TMB 3400 displayed higher specific XR, XDH and XK activities than TMB 3399. Hence, we have demonstrated that a combination of metabolic engineering and random mutagenesis was successful to generate a superior, xylose-utilizing S. cerevisiae, and uncovered distinctive physiological properties of the mutant.     

Ethanol production by Saccharomyces cerevisiae in biofilm reactors

Biofilms are natural forms of cell immobilization in which microorganisms attach to solid supports. At ISU, we have developed plastic composite-supports (PCS) (agricultural material (soybean hulls or oat hulls), complex nutrients, and polypropylene) which stimulate biofilm formation and which supply nutrients to the attached microorganisms. Various PCS blends were initially evaluated in repeated-batch culture-tube fermentation with Saccharomyces cerevisiae (ATCC 24859) in low organic nitrogen medium. The selected PCS (40% soybean hull, 5% soybean flour, 5% yeast extract-salt and 50% polypropylene) was then used in continuous and repeated-batch fermentation in various media containing lowered nitrogen content with selected PCS. During continuous fermentation, S. cerevisiae demonstrated two to 10 times higher ethanol production in PCS bioreactors than polypropylene-alone support (PPS) control. S. cerevisiae produced 30 g L⁻¹ ethanol on PCS with ammonium sulfate medium in repeated batch fermentation, whereas PPS-control produced 5 g L⁻¹ ethanol. Overall, increased productivity in low cost medium can be achieved beyond conventional fermentations using this novel bioreactor design. Received 20 May 1997/ Accepted in revised form 29 August 1997     

Influence of magnesium concentration on growth,ethanol and xylitol production by Pichia stipitis NRRL Y-7124

Summary The effect of Mg⁺² on Pichia stipitis growth and ethanol production was studied under condition of constant oxygen uptake rate (OUR) . Biomass/xylose and biomass/Mg⁺² yields increased with Mg⁺² concentration with a maximum value at Mg⁺² 4mM, ethanol being the main product obtained. At low Mg⁺² levels (ImM) 49 % of carbon flux to ethanol was redirected to xylitol production, accomplished through NADH intracellular accumulation.     

Comparison of industrial yeast strains for fermentation of spent sulphite pulping liquor fortified with wood hydrolysate

Ethanol production from spent sulphite pulping liquor (SSL) was compared for four different yeasts. A second strain of S. cerevisiae as well as a 2-deoxyglucose-resistant strain formed through protoplast fusions between S. uvarum and S. diastaticus produced up to 27% more ethanol from SSL fortified with hydrolysis sugars than was produced by S. cerevisiae. The incremental improvement in ethanol yield appeared to vary with the degree of fortification, ranging from 5.8% for unfortified SSL, to 27% for the highest level of fortification tested. Decreasing fermentation rates were observed for SSL fortified with glucose, mannose and galactose, respectively. Sugar uptake rates in SSL fortified with glucose, galactose and mannose were 6.8, 2.8 and 2.0 g L⁻¹ h⁻¹, respectively. However, when these sugars were fermented along with a glucose cosubstrate, the rate at which the combined glucose/mannose medium was fermented was nearly identical to that of the glucose control. Received 18 April 1996/ Accepted in revised form 27 August 1996     

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.     

High alcohol production by repeated batch fermentation using an immobilized osmotolerant Saccharomyces cerevisiae

A repeated batch fermentation system was used to produce ethanol using an osmotolerant Saccharomyces cerevisiae (VS₃) immobilized in calcium alginate beads. For comparison free cells were also used to produce ethanol by repeated batch fermentation. Fermentation was carried for six cycles with 125, 250 or 500 beads using 150, 200 or 250 g glucose L⁻¹ at 30°C. The maximum amount of ethanol produced by immobilized VS₃ using 150 g L⁻¹ glucose was only 44 g L⁻¹ after 48 h, while the amount of ethanol produced by free cells in the first cycle was 72 g L⁻¹. However in subsequent fed batch cultures more ethanol was produced by immobilized cells compared to free cells. The amount of ethanol produced by free cells decreased from 72 g L⁻¹ to 25 g L⁻¹ after the fourth cycle, while that of immobilized cells increased from 44 to 72 g L⁻¹. The maximum amount of ethanol produced by immobilized VS₃ cells using 150, 200 and 250 g glucose L⁻¹ was 72.5, 93 and 87 g ethanol L⁻¹ at 30°C. Journal of Industrial Microbiology & Biotechnology (2000) 24, 222–226. Received 16 September 1999/ Accepted in revised form 22 December 1999     

Ethanol production from rice hull using Pichia stipitis and optimization of acid pretreatment and detoxification processes

The goal of this study was to produce ethanol from rice hull hydrolysates (RHHs) using Pichia stipitis strains and to optimize dilute acid hydrolysis and detoxification processes by response surface methodology (RSM). The optimized conditions were found as 127.14°C, solid:liquid ratio of 1:10.44 (w/v), acid ratio of 2.52% (w/v), and hydrolysis time of 22.01 min. At these conditions, the fermentable sugar concentration was 21.87 g/L. Additionally, the nondetoxified RHH at optimized conditions contained 865.2 mg/L phenolics, 24.06 g/L fermentable sugar, no hydroxymethylfurfural (HMF), 1.62 g/L acetate, 0.36 g/L lactate, 1.89 g/L glucose, and 13.49 g/L fructose + xylose. Furthermore, RHH was detoxified with various methods and the best procedures were found to be neutralization with CaO or charcoal treatment in terms of the reduction of inhibitory compounds as compared to nondetoxified RHH. After detoxification procedures, the content of hydrolysates consisted of 557.2 and 203.1 mg/L phenolics, 19.7 and 21.60 g/L fermentable sugar, no HMF, 0.98 and 1.39 g/L acetate, 0 and 0.04 g/L lactate, 1.13 and 1.03 g/L glucose, and 8.46 and 12.09 g/L fructose + xylose, respectively. Moreover, the base‐line mediums (control), and nondetoxified and detoxified hydrolysates were used to produce ethanol by using P. stipitis strains. The highest yields except that of base‐line mediums were achieved using neutralization (35.69 and 38.33% by P. stipitis ATCC 58784 and ATCC 58785, respectively) and charcoal (37.55% by P. stipitis ATCC 58785) detoxification methods. Results showed that the rice hull can be utilized as a good feedstock for ethanol production using P. stipitis. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:872–882, 2016     

乙醇耐受性酿酒酵母菌株选育的研究进展

酿酒酵母是工业发酵生产乙醇的重要菌种,但是其发酵产物乙醇对酿酒酵母有明显的抑制作用.选育乙醇耐受性酿酒酵母是克服高浓度乙醇的抑制作用,提高乙醇产量的一条重要途径.本文对近年来国内外选育乙醇耐受性酵母的研究作一综述,旨在为乙醇耐受性酵母的选育提供参考.     

高效发酵木糖生产乙醇酵母菌株的构建

获得高效发酵木糖生产乙醇的酵母菌株是木质纤维素生物转化生产燃料乙醇的重要前提。在4%乙醇驯化的基础上,选择了乙醇耐性提高的休哈塔假丝酵母（Candida shehatae）CICC1766菌株进一步进行紫外诱变,得到了木糖发酵性能较强的呼吸缺陷型突变体,并与乙醇发酵性能良好的酿酒酵母（Saccharomyces cerevisiae）ATCC4126进行原生质体融合。采用单亲灭活法对休哈塔假丝酵母原生质体进行紫外灭活,在聚乙二醇（PEG）诱导下融合,对得到的融合子进行木糖发酵能力测定,选择到了一株能够更好地利用木糖产乙醇,并且木糖发酵性能比亲本得到明显提高的融合子F6,此融合子发酵50 g/L木糖,最高乙醇浓度达到18.75g/L,乙醇得率为0.375,达到理论转化值0.511的73.4%。与原始出发菌株CICC1766相比,乙醇产量提高了28%。     

Ethanol production from nonsterilized carob pod extract by free and immobilized Saccharomyces cerevisiae cells using fed-batch culture

The production of ethanol from carob pod extract by free and immobilized Saccharomyces cerevisiae cells in batch and fed-batch culture was investigated. Fed-batch culture proved to be a better fermentation system for the production of ethanol than batch culture. In fed-batch culture, both free and immobilized S. cerevisiae cells gave the same maximum concentration (62 g/L) of final ethanol at an initial sugar concentration of 300 g/L and F = 167 mL/h. The maximum ethanol productivity (4.4 g/L h) was obtained with both free and immobilized cells at a substrate concentration of 300 g/L and F = 334 mL/h. In repeated fed-batch culture, immobilized S. cerevisiae cells gave a higher overall ethanol concentration compared with the free cells. The immobilized S. cerevisiae cells in Ca-alginate beads retained their ability to produce ethanol for 10 days. (c) 1994 John Wiley & Sons, Inc.     

Ethanol production from acid hydrolysates based on the construction and demolition wood waste using Pichia stipitis

The feasibility of ethanol production from the construction and demolition (C&D) wood waste acid hydrolysates was investigated. The chemical compositions of the classified C&D wood waste were analyzed. Concentrated sulfuric acid hydrolysis was used to obtain the saccharide hydrolysates and the inhibitors in the hydrolysates were also analyzed. The C&D wood waste composed of lumber, plywood, particleboard, and medium density fiberboard (MDF) had polysaccharide (cellulose, xylan, and glucomannan) fractions of 60.7-67.9%. The sugar composition (glucose, xylose, and mannose) of the C&D wood wastes varied according to the type of wood. The additives used in the wood processing did not appear to be released into the saccharide solution under acid hydrolysis. Although some fermentation inhibitors were detected in the hydrolysates, they did not affect the ethanol production by Pichia stipitis. The hexose sugar-based ethanol yield and ethanol yield efficiency were 0.42-0.46 g ethanol/g substrate and 84.7-90.7%, respectively. Therefore, the C&D wood wastes dumped in landfill sites could be used as a raw material feedstock for the production of bioethanol.     

Ethanol production from paper sludge by simultaneous saccharification and co‐fermentation using recombinant xylose‐fermenting microorganisms

Simultaneous saccharification and co‐fermentation (SSCF) of waste paper sludge to ethanol was investigated using two recombinant xylose‐fermenting microbes: Zymomonas mobilis 8b and Saccharomyces cerevisiae RWB222. S. cerevisiae RWB222 produced over 40 g/L ethanol with a yield of 0.39 g ethanol/g carbohydrate on paper sludge at 37°C, while similar titers and yields were achieved by Z. mobilis 8b at 30°C. Both S. cerevisiae RWB222 and Z. mobilis 8b exhibited decreasing cell viability at 37°C when producing over 40 g/L ethanol. A high ethanol concentration can account for S. cerevisiae RWB222 viability loss, but ethanol concentration was not the only factor influencing Z. mobilis 8b viability loss at 37°C. Over 3 g/L residual glucose was observed at the end of paper sludge SSCF by Z. mobilis 8b, and a statistical analysis revealed that a high calcium concentration originating from paper sludge, a high ethanol concentration, and a high temperature were the key interactive factors resulting in glucose accumulation. The highest ethanol yields were achieved by SSCF of paper sludge with S. cerevisiae RWB222 at 37°C and Z. mobilis 8b at 30°C. With good sugar consumption at 37°C, S. cerevisiae RWB222 was able to gain an improvement in the polysaccharide to sugar yield compared to that at 30°C, whereas Z. mobilis 8b at 30°C had a lower polysaccharide to sugar yield, but a higher sugar to ethanol yield than S. cerevisiae. Both organisms under optimal conditions achieved a 19% higher overall conversion of paper sludge to ethanol than the non‐xylose utilizing S. cerevisiae D5A at its optimal process temperature of 37°C. Biotechnol. Bioeng. 2010;107: 235–244. © 2010 Wiley Periodicals, Inc.