Consolidated bioprocessing strategy for ethanol production from Jerusalem artichoke tubers by Kluyveromyces marxianus under high gravity conditions

Aims: Developing an innovative process for ethanol fermentation from Jerusalem artichoke tubers under very high gravity (VHG) conditions. Methods and Results: A consolidated bioprocessing (CBP) strategy that integrated inulinase production, saccharification of inulin contained in Jerusalem artichoke tubers and ethanol production from sugars released from inulin by the enzyme was developed with the inulinase‐producing yeast Kluyveromyces marxianus Y179 and fed‐batch operation. The impact of inoculum age, aeration, the supplementation of pectinase and nutrients on the ethanol fermentation performance of the CBP system was studied. Although inulinase activities increased with the extension of the seed incubation time, its contribution to ethanol production was negligible because vigorously growing yeast cells harvested earlier carried out ethanol fermentation more efficiently. Thus, the overnight incubation that has been practised in ethanol production from starch‐based feedstocks is recommended. Aeration facilitated the fermentation process, but compromised ethanol yield because of the negative Crabtree effect of the species, and increases the risk of contamination under industrial conditions. Therefore, nonaeration conditions are preferred for the CBP system. Pectinase supplementation reduced viscosity of the fermentation broth and improved ethanol production performance, particularly under high gravity conditions, but the enzyme cost should be carefully balanced. Medium optimization was performed, and ethanol concentration as high as 94·2 g l^?1 was achieved when 0·15 g l^?1 K₂HPO₄ was supplemented, which presents a significant progress in ethanol production from Jerusalem artichoke tubers. Conclusions: A CBP system using K. marxianus is suitable for efficient ethanol production from Jerusalem artichoke tubers under VHG conditions. Significance and Impact of the Study: Jerusalem artichoke tubers are an alternative to grain‐based feedstocks for ethanol production. The high ethanol concentration achieved using K. marxianus with the CBP system not only saves energy consumption for ethanol distillation, but also significantly reduces the amount of waste distillage discharged from the distillation system.     

Improved ethanol production in Jerusalem artichoke tubers by overexpression of inulinase gene in Kluyveromyces marxianus

Ethanol production from Jerusalem artichoke tubers through a consolidated bioprocessing (CBP) strategy using the inulinase-producing yeast Kluyveromyces marxianus is an economical and competitive than that from a grainbased feedstock. However, poor inulinase production under ethanol fermentation conditions significantly prolongs the fermentation time and compromises ethanol productivity. Improvement of inulinase activity appears to be promising for increasing ethanol production from Jerusalem artichoke tubers by CBP. In the present study, expression of the inulinase gene INU with its own promoter in K. marxianus (K/INU2) was explored using the integrative cassette. Overexpression of INU was explored using chromosome integration via the HO locus of the yeast. Inulinase activity and ethanol were determined from inulin and Jerusalem artichoke tubers under fed-batch operation. Inulinase activity was 114.9 U/mL under aerobic conditions for K/INU2, compared with 52.3 U/mL produced by the wild type strain. Importantly, inulinase production was enhanced in K/INU2 under ethanol fermentation conditions. When using 230 g/L inulin and 220 g/L Jerusalem artichoke tubers as substrates, inulinase activities of 3.7 and 6.8 U/mL, respectively, were measured using K/INU2, comparing favorably with 2.4 and 3.1 U/mL, respectively, using the wide type strain. Ethanol concentration and productivity for inulin were improved by the recombinant yeast to 96.2 g/L and 1.34 g/L/h, respectively, vs 93.7 g/L and 1.12 g/L/h, respectively, by the wild type strain. Ethanol concentration and productivity improvements for Jerusalem artichoke tubers were 69 g/L and 1.44 g/L/h, respectively, from the recombinant strain vs 62 g/L and 1.29 g/L/h, respectively, from the wild type strain.     

Ethanol fermentation with Kluyveromyces marxianus from Jerusalem artichoke grown in salina and irrigated with a mixture of seawater and freshwater

Aims: To study fuel ethanol fermentation with Kluyveromyces marxianus ATCC8554 from Jerusalem artichoke (Helianthus tuberosus) grown in salina and irrigated with a mixture of seawater and freshwater. Methods and Results: The growth and ethanol fermentation of K. marxianus ATCC8554 were studied using inulin as substrate. The activity of inulinase, which attributes to the hydrolysis of inulin, the main carbohydrate in Jerusalem artichoke, was monitored. The optimum temperatures were 38°C for growth and inulinase production, and 35°C for ethanol fermentation. Aeration was not necessary for ethanol fermentation with the K. marxianus from inulin. Then, the fresh Jerusalem artichoke tubers grown in salina and irrigated with 25% and 50% seawater were further examined for ethanol fermentation with the K. marxianus, and a higher ethanol yield was achieved for the Jerusalem artichoke tuber irrigated with 25% seawater. Furthermore, the dry meal of the Jerusalem artichoke tubers irrigated with 25% seawater was examined for ethanol fermentation at three solid concentrations of 200, 225 and 250 g l^?1, and the highest ethanol yield of 0·467, or 91·5% of the theoretical value of 0·511, was achieved for the slurry with a solid concentration of 200 g l^?1. Conclusions: Halophilic Jerusalem artichoke can be used for fuel ethanol production. Significance and Impact of the Study: Halophilic Jerusalem artichoke, not competing with grain crops for arable land, is a sustainable feedstock for fuel ethanol production.     

Efficient production of butyric acid from Jerusalem artichoke by immobilized Clostridium tyrobutyricum in a fibrous-bed bioreactor

Butyric acid is an important specialty chemical with wide industrial applications. The feasible large-scale fermentation for the economical production of butyric acid requires low-cost substrate and efficient process. In the present study, butyric acid production by immobilized Clostridium tyrobutyricum was successfully performed in a fibrous-bed bioreactor using Jerusalem artichoke as the substrate. Repeated-batch fermentation was carried out to produce butyric acid with a high butyrate yield (0.44 g/g), high productivity (2.75 g/L/h) and a butyrate concentration of 27.5 g/L. Furthermore, fed-batch fermentation using sulfuric acid pretreated Jerusalem artichoke hydrolysate resulted in a high butyric acid concentration of 60.4 g/L, with the yield of 0.38 g/g and the selectivity of ∼85.1 (85.1 g butyric acid/g acetic acid). Thus, the production of butyric acid from Jerusalem artichoke on a commercial scale could be achieved based on the system developed in this work.     

Citric acid production from extract of Jerusalem artichoke tubers by the genetically engineered yeast Yarrowia lipolytica strain 30 and purification of citric acid

In this study, citric acid production from extract of Jerusalem artichoke tubers by the genetically engineered yeast Yarrowia lipolytica strain 30 was investigated. After the compositions of the extract of Jerusalem artichoke tubers for citric acid production were optimized, the results showed that natural components of extract of Jerusalem artichoke tubers without addition of any other components were suitable for citric acid production by the yeast strain. During 10 L fermentation using the extract containing 84.3 g L^?1 total sugars, 68.3 g L^?1 citric acid was produced and the yield of citric acid was 0.91 g g^?1 within 336 h. At the end of the fermentation, 9.2 g L^?1 of residual total sugar and 2.1 g L^?1 of reducing sugar were left in the fermented medium. At the same time, citric acid in the supernatant of the culture was purified. It was found that 67.2 % of the citric acid in the supernatant of the culture was recovered and purity of citric acid in the crystal was 96 %.     

鹰嘴豆孢克鲁维酵母利用菊芋原料同步糖化与发酵生产乙醇

菊芋含有大量的菊粉多糖,且种植简单、产量高,是极具开发价值的替代玉米等粮食作物生产燃料乙醇的原料。文中研究了鹰嘴豆孢克鲁维酵母Y179利用菊芋原料同步糖化与发酵生产乙醇。鹰嘴豆孢克鲁维酵母Y179具有高效分泌菊粉酶的能力,摇瓶试验显示Y179酵母能够利用完全由菊芋原料配制而成的培养基良好生长并发酵产生乙醇。通气及温度对乙醇产量影响明显,相对厌氧环境对Y179酵母发酵产乙醇具有促进作用,30℃发酵温度相对37℃和42℃更有利于乙醇产量提高。种子液培养时间及接种量对乙醇产量影响较小。在5 L发酵罐中以10%(V/V)量接入预培养36 h的Y179种子液,发酵液完全由菊芋干粉配制而成,总糖含量22%(W/V),30℃不通气,300 r/min搅拌,发酵144 h时,乙醇浓度达到12.3%(V/V),糖醇转化效率86.9%,糖利用率大于93.6%。初步研究结果显示鹰嘴豆孢克鲁维酵母Y179在利用菊芋原料生产乙醇方面具有良好应用前景。     

Efficient production of l-lactic acid from hydrolysate of Jerusalem artichoke with immobilized cells of Lactococcus lactis in fibrous bed bioreactors

Hydrolysate of Jerusalem artichoke was applied for the production of l-lactic acid by immobilized Lactococcus lactis cells in a fibrous bed bioreactor system. Preliminary experiments had indicated that the high quality hydrolysate, which was derived from the 40min acid treatment at 95°C and pH 1.8, was sufficient to support the cell growth and synthesis of l-lactic acid. With the addition of 5g/l yeast extract, the fermentative performance of free cell system was evidently improved. After the basal settlement of hydrolysate based fermentation, the batch mode and the fed-batch mode fermentation were carried out in the free cell system and the fibrous bed bioreactor system, respectively. In all cases the immobilized cells presented the superior ability to produce l-lactic acid. The comparison of batch mode and fed-batch mode also indicated that the growth-limiting feeding strategy could reduce the lag phase of fermentation process and enhance the production of l-lactic acid. The achieved maximum concentration of l-lactic acid was 142g/l in the fed-batch mode. Subsequent repeated-batch fermentation of the fibrous bed bioreactor system had further exhibited the persistence and stability of this system for the high production of l-lactic acid in a long term. Our work suggested the great potential of the fibrous bed bioreactor system and hydrolysate of J. artichoke in the economical production of l-lactic acid at industrial scale.     

一步法发酵菊芋生产乙醇

利用马克斯克鲁维酵母(Kluyveromyces marxianus)YX01具有菊粉酶生产能力且乙醇发酵性能良好的特点,直接发酵菊粉生成乙醇.在摇瓶中考察了该菌株最适发酵温度,进而在2.5L发酵罐中考察了通气量和底物浓度的影响.实验结果表明:该菌株最适发酵温度为35℃;在通气量为50 mL/min和100 mL/min时菌体生长加快,发酵时间缩短,但在不通气条件下糖醇转化率明显提高;在菊粉浓度235 g/L时,发酵终点乙醇浓度达到92.2 g/L,乙醇对糖的得率为0.436,为理论值的85.5%.在此基础上,使用近海滩涂种植海水灌溉收获的菊芋为底物,以批式补料方式直接发酵菊芋干粉浓度为280 g/L的底物,发酵终点乙醇浓度为84.0 g/L,乙醇对糖的得率为0.405,为理论值的80.0%.这些研究工作,为以菊芋为原料的燃料乙醇技术开发奠定了基础.     

圆红冬孢酵母发酵菊芋块茎产油脂的研究

研究了圆红冬孢酵母Y4发酵菊芋块茎,菊芋品种及其处理方法对发酵产油的影响。结果表明,菊芋浸提汁、酸水解液或菊芋浆均可直接被圆红冬孢酵母Y4利用,发酵积累油脂,但白皮菊芋比紫皮菊芋更有利于油脂发酵。发酵菊芋浸提汁或酸水解液时,无需添加外源营养物,干菌体油脂含量可达到40%（w/w）;发酵菊芋浆时,白皮菊芋转化率达到12.1 g油/100 g去皮干菊芋。菊芋油脂发酵产品主要以16碳和18碳系脂肪酸为主,与常规植物油的脂肪酸组成相似,可作为制备生物柴油的新型替代原料。     

菊芋粕菊粉的酶法提取、组成及抗氧化活性研究

本研究拟应用酶法提取技术解决菊芋菊粉工业化生产中的废弃物——菊芋粕再利用程度低的问题,并评价菊芋粕菊粉的抗氧化活性功效。对菊芋粕菊粉的果胶酶酶法提取的最佳条件通过响应面法进行了优化,并对菊芋初次水提菊粉(primary water-extracted inulin,PWI)和二次酶提菊粉(secondary enzymatic-extracted inulin,SEI)的组成成分和抗氧化活性进行了比较分析。响应面法优化确定的菊芋粕菊粉最佳酶法提取条件为:pH4.5、提取温度50 ℃、酶底比7.5 U/g、提取时间2 h,该提取方法所得菊芋粕菊粉的得率为35.30%±0.85%,与传统热水浸提法相比菊粉得率提高38.16%。组成分析结果显示,SEI的总糖和菊粉含量均显著高于PWI( P <0.05)。在菊粉聚合度方面,PWI中蔗果三糖和蔗果四糖含量较高,而SEI中蔗果五糖、蔗果六糖及其以上聚合度菊粉的含量较高。此外,SEI的抗氧化活性优于PWI。因此,果胶酶辅助提取方法有望为菊芋粕菊粉的再利用难题提供新的解决思路。     

Microbial production of 2,3-butanediol from Jerusalem artichoke tubers by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

2,3-Butanediol is one of the promising bulk chemicals with wide applications. Its fermentative production has attracted great interest due to the high end concentration. However, large-scale production of 2,3-butanediol requires low-cost substrate and efficient fermentation process. In the present study, 2,3-butanediol production by Klebsiella pneumoniae from Jerusalem artichoke tubers was successfully performed, and various technologies, including separate hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF), were investigated. The concentration of target products reached 81.59 and 91.63 g/l, respectively after 40 h in batch and fed-batch SSF processes. Comparing with fed-batch SHF, the fed-batch SSF provided 30.3% higher concentration and 83.2% higher productivity of target products. The results showed that Jerusalem artichoke tuber is a favorable substrate for 2,3-butanediol production, and the application of fed-batch SSF for its conversion can result in a more cost-effective process.     

果糖及葡萄糖混合物为底物的丙酮丁醇发酵

旨在以果糖和葡萄糖混合物模拟能源作物菊芋块茎水解液发酵生产丁醇。在培养基初始pH 5.5,发酵过程不控制pH的混合糖发酵中,出现了发酵提前终止现象,终点残糖浓度达23.26 g/L,而丁醇产量仅5.51 g/L。进一步对比混合糖及葡萄糖、果糖不控制pH的发酵结果表明,导致这一现象的原因可能是有机酸毒性太大和pH太低。全程控制pH的混合糖发酵结果表明,高pH条件有利于提高糖利用率,但产酸多,丁醇产量较低;而低pH条件下发酵残糖较多,但丁醇产量相对较高。基于此,文中采用阶段性pH调控策略,即将发酵初期的pH控     

Enhanced propionic acid production from Jerusalem artichoke hydrolysate by immobilized Propionibacterium acidipropionici in a fibrous-bed bioreactor

Propionic acid is an important chemical that is widely used in the food and chemical industries. To enhance propionic acid production, a fibrous-bed bioreactor (FBB) was constructed and Jerusalem artichoke hydrolysate was used as a low-cost renewable feedstock for immobilized fermentation. Comparison of the kinetics of immobilized-cell fermentation using the FBB with those of fed-batch free-cell fermentation showed that immobilized-cell fermentation gave a much higher propionic acid concentration (68.5 vs. 40.6 g/L), propionic acid yield (0.434 vs. 0.379 g/g) and propionic acid productivity (1.55 vs. 0.190 g/L/h) at pH 6.5. Furthermore, repeated batch fermentation, carried out to evaluate the stability of the FBB system, showed that long-term operation with a high average propionic acid yield of 0.483 g/g, high productivity of 3.69 g/L/h and propionic acid concentration of 26.2 g/L were achieved in all eight repeated batches during fermentation for more than 200 h. It is thus concluded that the FBB culture system can be utilized to realize the economical production of propionic acid from Jerusalem artichoke hydrolysate during long-term operation.     

Thermotolerant Kluyveromyces marxianus and Saccharomyces cerevisiae strains representing potentials for bioethanol production from Jerusalem artichoke by consolidated bioprocessing

Thermotolerant inulin-utilizing yeast strains are desirable for ethanol production from Jerusalem artichoke tubers by consolidated bioprocessing (CBP). To obtain such strains, 21 naturally occurring yeast strains isolated by using an enrichment method and 65 previously isolated Saccharomyces cerevisiae strains were investigated in inulin utilization, extracellular inulinase activity, and ethanol fermentation from inulin and Jerusalem artichoke tuber flour at 40?°C. The strains Kluyveromyces marxianus PT-1 (CGMCC AS2.4515) and S. cerevisiae JZ1C (CGMCC AS2.3878) presented the highest extracellular inulinase activity and ethanol yield in this study. The highest ethanol concentration in Jerusalem artichoke tuber flour fermentation (200?g?L(-1)) at 40?°C achieved by K. marxianus PT-1 and S. cerevisiae JZ1C was 73.6 and 65.2?g?L(-1), which corresponded to the theoretical ethanol yield of 90.0 and 79.7?%, respectively. In the range of 30 to 40?°C, temperature did not have a significant effect on ethanol production for both strains. This study displayed the distinctive superiority of K. marxianus PT-1 and S. cerevisiae JZ1C in the thermotolerance and utilization of inulin-type oligosaccharides reserved in Jerusalem artichoke tubers. It is proposed that both K. marxianus and S. cerevisiae have considerable potential in ethanol production from Jerusalem artichoke tubers by a high temperature CBP.     

Ethanol production from Jerusalem artichoke tubers (Helianthus tuberosus) using Kluyveromyces marxianus and Saccharomyces rosei

This article examines the potential of Jerusalem artichoke as a source for ethanol and single-cell protein SCP. In addition, experimental results are presented on batch fermentation kinetics employing two strains of Kluyveromyces marxianus and one strain of Saccharomyces rosei grown on the extract derived from the tubers of Jerusalem artichoke. Of the three cultures examined, Kluyveromyces marxianus UCD (FST) 55-82 was found to be the best producer of ethanol grown in a simple medium at 35 degrees C. The ethanol production was found to be growth-associated having a mu(max) = 0.41. h(-1) and the ethanol and biomass yields were determined to be Y(p/s) = 0.45 (88% of the theoretical) and Y(x/s) = 0.04 with 92% of the original sugars utilized. On the basis of carbohydrate yields of Jerusalem artichoke reported in the literature and these batch kinetic studies with K. maxxianus, the calculated ethanol yields were found to range from 1400 kg ethanol acre (-1) yr(-1)to a maximum of 2700 kg ethanol acre (-1) yr(-1). The SCP yields for K. marxianus were calculated to range between 130 to 250 kg dry wt cell acre (-1) yr(-1). The potential for developing an integrated process to produce ethanol and SCP is also discussed.     

Batch and continuous solid-phase fermentation of Jerusalem artichoke tubers

Two strains of Kluyveromyces marxianus were evaluated for their ability to ferment Jerusalem artichoke tuber pulp to ethanol under pH levels ranging from 2.0–6.3. Bacterial contamination was prevented in batch, solid-phase fermentation when pulp was initially adjusted to pH 3.5 or less, and maximal yeast populations occurred at pH 3.0–3.5. Fermentation times were also shortest for both yeast (13–18 h) and ethanol (48–64 h) production when pulp pH was in this range. However, ethanol yields (41–53% of theoretical) and fermentation efficiencies (68–78%) were somewhat lower than expected, with only 6.6–7.2% (v/v) ethanol produced by strain Y-1598 and 5.7–6.9% produced by strain Y-1550. Based on these parameters, the continuous solid-phase fermentor was operated for 396 h using strain Y-1598. The pH of pulp entering the fermentor was adjusted to 2.5 to compensate for partial neutralization by the mild steel of the fermentor. This resulted in fermenting pulp with a pH of 3.0–3.5, and therefore no contamination. Pulp exiting the fermentor after 72 h contained 6.9 × 10⁸ yeast cells/ml and 7.3% ethanol, which represented 55.9% of the theoretical yield and a fermentation efficiency of 73.3%. Further modifications (partial acid hydrolysis, finer grinding, etc.) should permit higher yields.     

Optimization of alcohol production from Jerusalem artichokes

Summary Fermentation of Jerusalem artichoke extracts by yeasts with inulinase activity is possible, without prior hydrolysis or sterilization, if carried out at pH 3.5. For semi-continuous production, a small amount of the yeast harvested at the end of the previous fermentation can be used as the subsequent inoculant. Up to 75 hl of alcohol per ha can be obtained by this process under favorable energetic conditions. A partial inhibition of the fermentation was detected in extracts obtained from tubers harvested too early; this inhibition seems unrelated to the extent of polymerization of sugars.     

Contributo Alla Flora Dell'alto Adige

In order to obtain a high ethanol yield from the Jerusalem artichoke raw extract and reduce the fermentation cost, we have engineered a new recombinant Saccharomyces cerevisiae strain that could produce ex-inulinase. The response surface methodology based on Plackett–Burman and Box–Behnken design was used to optimize the medium for the ethanol production from the Jerusalem artichoke raw extracts by the recombinant strain. In the first optimization step, Plackett–Burman design was employed to select significant factors, including concentrations of yeast extract, inoculum, and MgSO₄·7H₂O. In the second step, the steepest ascent experiment was carried out to determine the center point with the three significant factors; the selected combinations were further optimized using the Box–Behnken design. The maximum ethanol production rate was predicted at 91.1 g/l, which was based on a medium consisting of yeast extract 9.24 g/l, inoculum 39.8 ml/l, and MgSO₄·7H₂O 0.45 g/l. In the validating experiment, the ethanol fermentation rate reached 102.1 g/l, closely matching the predicted rate.     

Simultaneous saccharification of inulin and ethanol fermentation by recombinantSaccharomyces cerevisiae secreting inulinase

VariousSaccharomyces cerevisiae strains were transformed with a 2 μ-based multicopy expression plasmid, pYIGP, carryingKluyveromyces marxianus inulinase gene under the control ofGAPDH promoter. Among them two strains, SEY2102 and 2805, showed high levels of cell growth and inulinase expression, and were selected to study their fermentation properties on inulin. Jerusalem artichoke inulin was more effective for cell growth (10∼11 g-dry wt./L at 48 hr) and inulinase expression (1.0 units/mL with SEY2102/pYIGP and 2.5 units/mL with 2805/pYIGP) than other inulin sources such as dahlia and chicory. It was also found that maximal ethanol production of 9 g/L was obtained from Jerusalem artichoke inulin at the early stationary phase (around 30 hr), indicating that recombinantS. cerevisiae cells secreting exoinulinase could be used for the simultaneous saccharification of inulin and ethanol fermentation.     

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