Fructose syrups and ethanol production by selective fermentation of inulin

Jerusalem artichoke is a favorable substrate for inulin or fructose syrup production. The sugar content and the fructose ratio of inulin depend on various factors, particularly on the date of harvest. Incomplete fermentation of extracts by selected yeasts allows the production of inulin with increased fructose content. The yeast strains (Saccharomyces cerevisiae, S. diastaticus...) are chosen for their ability to ferment sucrose and inulin small polymers, but not easily inulin large polymers. A good increase in the fructose ratio and a good yield in residual sugars can be obtained with the better strains. After fermentation and acid or enzymatic hydrolysis, extracts from early and late harvested tubers lead to syrups of good quality containing up to 95% and 90% of fructose respectively. This fermentative enrichment process is competitive with others (for example, chromatographic enrichment), is appropriate to raw extracts, simplifies the purification steps, and also permits the simultaneous benefit of production of by-products in the form of ethanol and yeast (in addition to the pulps). Unhydrolyzed inulin polymers with high fructose content can be recovered by this selective fermentation.     

Inulin enrichment by fermentation in a flocculating yeast reactor

Summary Simultaneous production of ethanol and fructose enriched syrups was obtained from Jerusalem artichoke extract using a Saccharomyces diastaticus flocculating yeast in a continuous gas-lift reactor with internal biomass recycle. This allowed the production of 42 g/L of ethanol and 70 g/L of inulin containing up to 92% fructose (fructose/glucose ratio of 11). These results can be compared to the batch and chemostat fermentations which gave a higher ethanol concentration but a lower fructose enrichment. Mass transfert limitations can explain both the productivity decrease and the selectivity improvement in the gas-lift reactor.     

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.     

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.     

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.     

Considerazioni su Gelsi Ingialliti per Fame

Jerusalem artichoke (Helianthus tuberosus L.), an important crop, containing over 50% inulin in its tubers on a dry weight basis is an agricultural and industrial crop with a great potential for production of ethanol and industrial products. Inulin is a good substrate for bioethanol production. Saccharomyces cerevisiae 6525 can produce high concentrations of ethanol, but it cannot synthesize inulinase. In this study, a new integration vector carrying inuA1 gene encoding exoinulinase was constructed and transformed into 18SrDNA site of industrial strain S. cerevisiae 6525. The obtained transformant, BR8, produced 1.1 U mL^? 1 inulinase activity within 72 h and the dry cell weight reached 12.3 g L^? 1 within 48 h. In a small-scale fermentation, BR8 produced 9.5% (v/v) ethanol, with a productivity rate of 0.385 g ethanol per gram inulin, while wild-type S. cerevisiae 6525 produced only 3.3% (v/v) ethanol in the same conditions. In a 5-L fermentation, BR8 produced 14.0% (v/v) ethanol in fermentation medium containing inulin and 1% (w/v) (NH4)₂SO₄. The engineered S. cerevisiae 6525 carrying inuA1 converted pure nonhydrolyzed inulin directly into high concentrations of ethanol.     

Fed-batch production of concentrated fructose syrup and ethanol using Saccharomyces cerevisiae ATCC 36859

A fed-batch process is used for the production of concentrated pure fructose syrup and ethanol from various glucose/fructose mixtures by S. cerevisiae ATCC 36859. Applying this technique, glucose-free fructose syrups with over 250 g/l of this sugar were obtained using High Fructose Corn Syrup and hydrolyzed Jerusalem artichoke juice. By encouraging ethanol evaporation from the reactor and condensing it, a separate ethanol product with a concentration of up to 350 g/l was also produced. The rates of glucose consumption and ethanol production were higher than in classical batch ethanol fermentation processes.     

Consolidated ethanol production from Jerusalem artichoke tubers at elevated temperature by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> engineered with inulinase expression through cell surface display

Ethanol fermentation from Jerusalem artichoke tubers was performed at elevated temperatures by the consolidated bioprocessing strategy using Saccharomyces cerevisiae MK01 expressing inulinase through cell surface display. No significant difference was observed in yeast growth when temperature was controlled at 38 and 40 °C, respectively, but inulinase activity with yeast cells was substantially enhanced at 40 °C. As a result, enzymatic hydrolysis of inulin was facilitated and ethanol production was improved with 89.3 g/L ethanol produced within 72 h from 198.2 g/L total inulin sugars consumed. Similar results were also observed in ethanol production from Jerusalem artichoke tubers with 85.2 g/L ethanol produced within 72 h from 185.7 g/L total sugars consumed. On the other hand, capital investment on cooling facilities and energy consumption for running the facilities would be saved, since regular cooling water instead of chill water could be used to cool down the fermentation system.     

Kinetics of kojic acid fermentation byAspergillus flavus link S44-1 using sucrose as a carbon source under different pH conditions

Kojic acid production byAspergillus flavus strain S44-1 using sucrose as a carbon source was carried out in a 250-mL shake flask and a 2-L stirred tank fermenter. For comparison, production of kojic acid using glucose, fructose and its mixture was also carried out. Kojic acid production in shake flask fermentation was 25.8 g/L using glucose as the sole carbon source, 23.6 g/L with sucrose, and 6.4 g/L from fructose. Reduced kojic acid production (13.5 g/L) was observed when a combination of glucose and fructose was used as a carbon source. The highest production of kojic acid (40.2 g/L) was obtained from 150 g/L sucrose in a 2 L fermenter, while the lowest kojic acid production (10.3 g/L) was seen in fermentation using fructose as the sole carbon source. The experimental data from batch fermentation and resuspended cell system was analysed in order to form the basis for a kinetic model of the process. An unstructured model based on logistic and Luedeking-Piret equations was found suitable to describe the growth, substrate consumption, and efficiency of kojic acid production byA. flavus in batch fermentation using sucrose. From this model, it was found that kojic acid production byA. flavus was not a growth-associated process. Fermentation without pH control (from an initial culture pH of 3.0) showed higher kojic acid production than single-phase pH-controlled fermentation (pH 2.5, 2.75, and 3.0).     

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.     

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.     

Production of mannitol and lactic acid by fermentation with Lactobacillus intermedius NRRL B-3693

Lactobacillus intermedius B-3693 was selected as a good producer of mannitol from fructose after screening 72 bacterial strains. The bacterium produced mannitol, lactic acid, and acetic acid from fructose in pH-controlled batch fermentation. Typical yields of mannitol, lactic acid, and acetic acid from 250 g/L fructose were 0.70, 0.16, and 0.12 g, respectively per g of fructose. The fermentation time was greatly dependent on fructose concentration but the product yields were not dependent on fructose level. Fed-batch fermentation decreased the time of maximum mannitol production from fructose (300 g/L) from 136 to 92 h. One-third of fructose could be replaced with glucose, maltose, galactose, mannose, raffinose, or starch with glucoamylase (simultaneous saccharification and fermentation), and two-thirds of fructose could be replaced with sucrose. L. intermedius B-3693 did not co-utilize lactose, cellobiose, glycerol, or xylose with fructose. It produced lactic acid and ethanol but no acetic acid from glucose. The bacterium produced 21.3 +/- 0.6 g lactic acid, 10.5 +/- 0.3 g acetic acid, and 4.7 +/- 0.0 g ethanol per L of fermentation broth from dilute acid (15% solids, 0.5% H(2)SO(4), 121 degrees C, 1 h) pretreated enzyme (cellulase, beta-glucosidase) saccharified corn fiber hydrolyzate.     

Fructose production by Zymomonas mobilis in fed-batch culture with minimal sorbitol formation

Summary Fed-batch cultures of Zymomonas mobilis (UQM 2864), a mutant unable to metabolise fructose, grown on diluted sugar cane syrup (200 g/l sucrose) achieved yields of 90.5 g/l fructose and 48.3 g/l ethanol with minimal sorbitol formation and complete utilization of the substrate. The effect of inoculum size on sorbitol formation in the batch stage of fed-batch fermentation are reported. Fermentation of sucrose (350 g/l) supplemented with nutrients yielded 142 g/l fructose and 76.5 g/l ethanol. Some fructose product loss at high fructose concentrations was observed. The fed-batch fermentation process offers a method for obtaining high concentrations of fructose and ethanol from sucrose materials.     

Maltose-fructose co-fermentation by Lactobacillus brevis subsp. lindneri CB1 fructose-negative strain

The Lactobacillus brevis subsp. lindneri CB1 fructose-negative strain utilized fructose in co-fermentation with maltose or glucose. Compared to the maltose (17 g/l) fermentation, the simultaneous fermentation of maltose (10 g/l) and fructose (7 g/l) increased cell yield (A ₆₂₀from 2.6 to 3.3) and the concentrations of lactic acid and especially of acetic acid (from 2.45 g/l to 3.90 g/l), produced mannitol (1.95 g/l) and caused a decrease in the amount of ethanol (from 0.46 g/l to 0.08 g/l). The utilization of fructose depended on the continuous presence of maltose in the growth medium and the two carbohydrates were consumed in a molar ratio of about 2:1. The presence of tagatose (a fructose stereoisomer) partially inhibited fructose consumption and consequently caused a decrease of the end products of the co-metabolism. Since maltose was naturally present during sourdough fermentation, the addition of only 6 g fructose/kg wheat dough enabled the co-fermentation of maltose and fructose by L. brevis subsp. lindneri CB1. A higher titratable acidity and acetic acid concentration, and a reduced quotient of fermentation (2.7) were obtained by co-fermentation compared with normal sourdough fermentation. Some interpretations of the maltose-fructose co-fermentation are given.     

Production of Fructose and Ethanol from Cane Molasses Using Saccharomyces cerevisiae ATCC 36858

The purpose of this research was to study the possibility of the production of ethanol and enriched fructose syrups from sugar cane molasses using the yeast Saccharomyces cerevisiae ATCC 36858. In batch experiments with a total sugar concentration of between 96.7 g/l and 323.5 g/l, the fructose yield was above 90% of the theoretical value. The ethanol yield and volumetric productivity were in the range of 66% and 77% of the theoretical value, and between 0.53 g ethanol/l × h and 3.15 g ethanol/l × h, respectively. The fructose fraction in the carbohydrates content of the produced syrups was more than 95% when the total initial sugar concentration in the medium was below 273.8 g/l. Some oligosaccharides and glycerol were also produced in all tested media. The maximum amount of produced oligosaccharides including raffinose accounted for 13.4 g/l in the cane molasses medium with 323.5 g/l sugars in the initial phase of the fermentation process. The oligosaccharides produced and raffinose were completely consumed by the end of the fermentation process when the total initial sugar concentration was less than 191.3 g/l. The glycerol concentration was below 9.9 g/l. These findings are useful in the production of ethanol and high fructose syrups using sugar cane molasses.     

Production of fructose and ethanol from sugar beet molasses using Saccharomyces cerevisiae ATCC 36858

The production of enriched fructose syrups and ethanol from beet molasses using Saccharomyces cerevisiae ATCC 36858 was studied. In batch experiments with a total sugar concentration between 94.9 and 312.4 g/L, the fructose yield was above 93% of the theoretical value. The ethanol yield and volumetric productivity in the beet molasses media with sugar concentration below 276.2 g/L were in the range of 59-76% of theoretical value and between 0.48 and 2.97 g of ethanol/(L x h), respectively. The fructose fraction in the carbohydrates content of the produced syrups was more than 95% when the total initial sugar concentration in the medium was below 242.0 g/L. Some oligosaccharides and glycerol were also produced in all tested media. Raffinose and the produced oligosaccharides were completely consumed by the end of the fermentation process when the total initial sugar concentration was below 190.1 g/L. The glycerol concentration was below 16.1 g/L. The results could be useful for a potential industrial production of ethanol and high-fructose syrup from sugar beet molasses.     

丙酮丁醇梭菌发酵菊芋汁生产丁醇

对丙酮丁醇梭菌Clostridium acetobutylicum L7发酵菊芋汁酸水解液生产丁醇进行了初步研究。实验结果表明,以该水解液为底物生产丁醇,不需要添加氮源和生长因子。当水解液初始糖浓度为48.36 g/L时,其发酵性能与以果糖为碳源的对照组基本相同,发酵终点丁醇浓度为8.67 g/L,丁醇、丙酮和乙醇的比例为0.58∶0.36∶0.06,但与以葡萄糖为碳源的对照组相比,发酵时间明显延长,表明该菌株葡萄糖转运能力强于果糖。当水解液初始糖浓度提高到62.87 g/L时,发酵终点残糖浓度从3.09 g/L增加到3.26 g/L,但丁醇浓度却提高到11.21 g/L,丁醇、丙酮和乙醇的比例相应为0.64∶0.29∶0.05,表明适量糖过剩有助于C.acetobutylicum L7胞内代谢从丙酮合成向丁醇合成途径调节;继续提高水解液初始糖浓度,发酵终点残糖浓度迅速升高,丁醇生产的技术经济指标受到明显影响。     

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。     

Highly efficient production of <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid from chicory-derived inulin by <Emphasis Type="Italic">Lactobacillus bulgaricus</Emphasis>

Inulin is a readily available feedstock for cost-effective production of biochemicals. To date, several studies have explored the production of bioethanol, high-fructose syrup and fructooligosaccharide, but there are no studies regarding the production of d-lactic acid using inulin as a carbon source. In the present study, chicory-derived inulin was used for d-lactic acid biosynthesis by Lactobacillus bulgaricus CGMCC 1.6970. Compared with separate hydrolysis and fermentation processes, simultaneous saccharification and fermentation (SSF) has demonstrated the best performance of d-lactic acid production. Because it prevents fructose inhibition and promotes the complete hydrolysis of inulin, the highest d-lactic acid concentration (123.6 ± 0.9 g/L) with a yield of 97.9 % was obtained from 120 g/L inulin by SSF. Moreover, SSF by L. bulgaricus CGMCC 1.6970 offered another distinct advantage with respect to the higher optical purity of d-lactic acid (>99.9 %) and reduced number of residual sugars. The excellent performance of d-lactic acid production from inulin by SSF represents a high-yield method for d-lactic acid production from non-food grains.