Candida shehatae and Saccharomyces cerevisiae work synergistically to improve ethanol fermentation from sugarcane bagasse and rice straw hydrolysate in immobilized cell bioreactor

Sugarcane bagasse (SCB) and rice straw (RS), abundant lignocellulosic agro‐industrial residues in South‐East Asia, are potent feedstocks for bioethanol production as they contain significant amount of glucose and xylose monomers after fractionation and subsequent enzymatic hydrolysis. To simultaneously convert glucose and xylose to ethanol, it requires co‐cultivation of Saccharomyces cerevisiae and Candida shehatae which are hexose and pentose‐fermenting yeasts, respectively. Xylose‐fermenting strain grows slower than glucose‐fermenting one, therefore low efficiency of xylose‐to‐ethanol conversion was found. To enhance the efficiency of ethanol fermentation, the present work proposed to improve xylose assimilation by using co‐immobilization of two strains in a packed bed bioreactor and to increase oxygenation of the medium by applying a recycled batch system when the recycle stream was intervened by a mixing system in a naturally aerated vessel. Initially, conversion of glucose and xylose to ethanol using pure culture was investigated. Subsequently, influence of different immobilization techniques was investigated. Cells entrapment in Ca‐alginate beads provided considerably high ethanol yield over cells immobilized on delignified cellulose, and thus it was selected to use as inoculum in an immobilized cell bioreactor (ICB). The results showed that continuous ethanol production yielded 0.38 and 0.40 g/g corresponding to 74.5% and 78.4% theoretical yields from SCB and RS hydrolysate, respectively. However, recycled batch system produced significantly improved ethanol yield to 0.49 g/g and 0.50 g/g corresponding to 96.1% and 98.0% theoretical yields for SCB and RS hydrolysate, respectively. In this study, higher ethanol concentration and less unfermented sugar concentration was successfully achieved in the ICB with recycled batch system when using SCB and RS hydrolysate as the substrate.     

Ethanol production from sulphuric acid wood hydrolysate ofPinus radiata using free and immobilized cells ofPichia stipitis

Summary Ethanol was produced by a strain ofPichia stipitis adapted to an inhibitory acid wood hydrolysate ofPinus radiata. The best ethanol productivity for batch cultures was 0.21 g/l h at 0.7% ethanol. Varying culture conditions increased ethanol concentration to 0.76%, however the productivity decreased to 0.18 g/l h. A decrease in ethanol concentration in the culture fluid was noted late in the batch which suggested ethanol catabolism. Values of kinetic parameters (K _m,K _s, _max, andV _max) were evaluated for this system. The use of calcium alginate immobilized cells in a continuous-flow stirred tank reactor lead to enhanced fermentative performance, namely a maximum productivity of 0.27 g/l h and 1.13% ethanol yield. The immobilized cells in continuous flow reactors represent an attractive option for fermenting sugars released by sulphuric acid hydrolysis ofP. radiata wood.     

Evaluation of xylitol production from corn cob hemicellulose hydrolysate by Candida parapsilosis

Candida parapsilosis was grown for 59 h in a medium containing corn cob hydrolysate consisting of 50 g xylose l^–1, 3.0 g glucose l^–1, 2.0 g arabinose l^–1, and 0.9 g acetic acid l^–1. A biomass of 9.1 g l^–1 was produced with 36 g xylitol l^–1 and 2.5 g ethanol l^–1. In a medium containing 50 g xylose l^–1 instead of corn cob hydrolysate, the concentrations of cells, xylitol, and ethanol were 8.6 g l^–1, 33 g l^–1, and 0.2 g l^–1, respectively. The differences between two cultures were due to the glucose and arabinose in the corn cob hydrolysate stimulating growth and the low concentration of acetic acid stimulating xylitol production.     

Fermentation of xylose and rice straw hydrolysate to ethanol byCandida shehatae NCL-3501

Candida shehatae NCL-3501 utilized glucose and xylose efficiently in batch cultures. The specific rate of ethanol production was higher with mixtures of glucose and xylose (0.64–0.83 g g^–1 cells d^–1) compared to that with individual sugars (0.38–0.58 g g^–1 cells d^–1). Although the optimum temperature for growth was 30°C, this strain grew and produced appreciable levels of ethanol at 45°C. A stable ethanol yield (0.40–0.43 g g^–1 substrate utilized) was obtained between 10 g L^–1 and 80 g L^–1 of initial xylose concentration. Conversion efficiency was further improved by immobilization of the cells in calcium alginate beads. Free or immobilized cells ofC. shehatae NCL-3501 efficiently utilized sugars present in rice straw hemicellulose hydrolysate, prepared by two different methods, within 48 h. Ethanol yields of 0.45 g g^–1 and 0.5 g g^–1 from autohydrolysate, and 0.37 g g^–1 from acid hydrolysate were produced by free and immobilized cells, respectively.     

Evaluation of ethanol production by a new isolate of yeast during fermentation in synthetic medium and sugarcane bagasse hemicellulosic hydrolysate

A new xylose fermenting yeast was isolated from over-ripe banana by enrichment in xylose-containing medium. The phylogenetic analysis of ITS1-5.8S-ITS2 region sequences of ribosomal RNA of isolate BY2 revealed that it shows affiliation to genus Pichia and clades with Pichia caribbica. In batch fermentation, Pichia strain BY2 fermented xylose, producing 15 g l^?1 ethanol from 30 g l^?1 xylose under shaking conditions at 28°C, with ethanol yield of 0.5 g g^?1 and volumetric productivity of 0.31 g l^?1 h^?1. The optimum pH range for ethanol production from xylose by Pichia strain BY2 was 5–7. Pichia strain BY2 also produced 6.08 g l^?1 ethanol from 30 g l^?1 arabinose. Pichia strain BY2 can utilize sugarcane bagasse hemicellulose acid hydrolysate for alcohol production, efficiency of fermentation was improved by neutralization, and sequential use of activated charcoal adsorption method. Percent total sugar utilized and ethanol yield for the untreated hydrolysate was 17.14% w/v and 0.33 g g^?1, respectively, compared with 66.79% w/v and 0.45 g g^?1, respectively, for treated hemicellulose acid hydrolysate. This new yeast isolate showed ethanol yield of 0.45 g g^?1 and volumetric productivity of 0.33 g l^?1 h^?1 from sugarcane bagasse hemicellulose hydrolysate detoxified by neutralization and activated charcoal treatment, and has potential application in practical process of ethanol production from lignocellulosic hydrolysate.     

Production of ethanol from corn stover hemicellulose hydrolyzate using <Emphasis Type="Italic">Pichia stipitis</Emphasis>

Hemicellulose liquid hydrolyzate from dilute acid pretreated corn stover was fermented to ethanol using Pichia stipitis CBS 6054. The fermentation rate increased with aeration but the pH also increased due to consumption of acetic acid by Pichia stipitis. Hemicellulose hydrolyzate containing 34 g/L xylose, 8 g/L glucose, 8 g/L Acetic acid, 0.73 g/L furfural, and 1 g/L hydroxymethyl furfural was fermented to 15 g/L ethanol in 72 h. The yield in all the hemicellulose hydrolyzates was 0.37–0.44 g ethanol/g (glucose + xylose). Nondetoxified hemicellulose hydrolyzate from dilute acid pretreated corn stover was fermented to ethanol with high yields, and this has the potential to improve the economics of the biomass to ethanol process.     

Lactic acid production from cellulosic waste by immobilized cells of Lactobacillus delbrueckii

Industrial waste corn cob residue (from xylose manufacturing) without pretreatment was hydrolyzed by cellulase and cellobiase. The cellulosic hydrolysate contained 52.4 g l⁻¹ of glucose and was used as carbon source for lactic acid fermentation by cells of Lactobacillus delbrueckii ZU-S2 immobilized in calcium alginate gel beads. The final concentration of lactic acid and the yield of lactic acid from glucose were 48.7 g l⁻¹ and 95.2%, respectively, which were comparative to the results of pure glucose fermentation. The immobilized cells were quite stable and reusable, and the average yield of lactic acid from glucose in the hydrolysate was 95.0% in 12 repeated batches of fermentation. The suitable dilution rate of continuous fermentation process was 0.13 h⁻¹, and the yield of lactic acid from glucose and the productivity were 92.4% and 5.746 g l⁻¹ h⁻¹, respectively. The production of lactic acid by simultaneous saccharification and fermentation (SSF) process was carried out in a coupling bioreactor, the final concentration of lactic acid was 55.6 g l⁻¹, the conversion efficiency of lactic acid from cellulose was 91.3% and the productivity was 0.927 g l⁻¹ h⁻¹. By using fed-batch technique in the SSF process, the final concentration of lactic acid and the productivity increased to 107.6 g l⁻¹ and 1.345 g l⁻¹ h⁻¹, respectively, while the dosage of cellulase per gram substrate decreased greatly. This research work should advance the bioconversion of renewable cellulosic resources and reduce environmental pollution.     

Evaluation of fermentative potential of <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> ATCC 36907 in cellulosic and hemicellulosic sugarcane bagasse hydrolysates on xylitol and ethanol production

This paper evaluates the fermentative potential of Kluyveromyces marxianus grown in sugarcane bagasse cellulosic and hemicellulosic hydrolysates obtained by acid hydrolysis. Ethanol was obtained from a single glucose fermentation product, whereas xylose assimilation resulted in xylitol as the main product and ethanol as a by-product derived from the metabolism of this pentose. Fermentation performed in a simulated hydrolysate medium with a glucose concentration similar to that of the hydrolysate resulted in ethanol productivity (Qp?=?0.86 g L^?1 h^?1) that was tenfold higher than the one observed in the cellulosic hydrolysate. However, the use of hemicellulosic hydrolysate favored xylose assimilation in comparison with simulated medium with xylose and glucose concentrations similar to those found in this hydrolysate, without toxic compounds such as acetic acid and phenols. Under this condition, xylitol yield was 53.8 % higher in relation to simulated medium. Thus, the total removal of toxic compounds from the hydrolysate is not necessary to obtain bioproducts from lignocellulosic hydrolysates.     

Overcoming inhibitors in a hemicellulosic hydrolysate: improving fermentability by feedstock detoxification and adaptation of <Emphasis Type="Italic">Pichia stipitis</Emphasis>

In order to improve the fermentative efficiency of sugar maple hemicellulosic hydrolysates for fuel ethanol production, various methods to mitigate the effects of inhibitory compounds were employed. These methods included detoxification treatments utilizing activated charcoal, anion exchange resin, overliming, and ethyl acetate extraction. Results demonstrated the greatest fermentative improvement of 50% wood hydrolysate (v/v) by Pichia stipitis with activated charcoal treatment. Another method employed to reduce inhibition was an adaptation procedure to produce P. stipitis stains more tolerant of inhibitory compounds. This adaptation resulted in yeast variants capable of improved fermentation of 75% untreated wood hydrolysate (v/v), one of which produced 9.8 g/l ± 0.6 ethanol, whereas the parent strain produced 0.0 g/l ± 0.0 within the first 24 h. Adapted strains RS01, RS02, and RS03 were analyzed for glucose and xylose utilization and results demonstrated increased glucose and decreased xylose utilization rates in comparison to the wild type. These changes in carbohydrate utilization may be indicative of detoxification or tolerance activities related to proteins involved in glucose and xylose metabolism.     

Isolation and Characterization of Xylitol-Producing Yeasts from the Gut of Colleopteran Insects

A total of 35 yeasts were isolated from the gut of beetles collected from Hyderabad city, India. Twenty of these yeasts utilized xylose as a sole carbon source but only 12 of these converted xylose to xylitol. The ability to convert xylose to xylitol varied among the isolates and ranged from 0.12 to 0.58 g/g xylose. Based on the phenotypic characteristics and phylogenetic analysis of the D1/D2 domain sequence of 26S rRNA gene, these isolates were identified as members of Pichia, Candida, Issatchenkia, and Clavispora. Strain YS 54 (CBS 10446), which was phylogenetically similar to Pichia caribbica and which formed hat-shaped ascospore characteristics of the genus Pichia, was the best xylitol producer (0.58 g xylitol/g xylose). YS 54 was also capable of producing xylitol from sugarcane bagasse hydrolysate and the efficiency of conversion was 0.32 g xylitol/g xylose after 20 cycles of adaptation in medium containing sugarcane bagasse hydrolysate.     

Ethanol production from corn cob hydrolysates by <Emphasis Type="Italic">Escherichia coli</Emphasis> KO11

Corn cob hydrolysates, with xylose as the dominant sugar, were fermented to ethanol by recombinant Escherichia coli KO11. When inoculum was grown on LB medium containing glucose, fermentation of the hydrolysate was completed in 163 h and ethanol yield was 0.50 g ethanol/g sugar. When inoculum was grown on xylose, ethanol yield dropped, but fermentation was faster (113 h). Hydrolysate containing 72.0 g/l xylose and supplemented with 20.0 g/l rice bran was readily fermented, producing 36.0 g/l ethanol within 70 h. Maximum ethanol concentrations were not higher for fermentations using higher cellular concentration inocula. A simulation of an industrial process integrating pentose fermentation by E. coli and hexose fermentation by yeast was carried out. At the first step, E. coli fermented the hydrolysate containing 85.0 g/l xylose, producing 40.0 g/l ethanol in 94 h. Baker's yeast and sucrose (150.0 g/l) were then added to the spent fermentation broth. After 8 h of yeast fermentation, the ethanol concentration reached 104.0 g/l. This two-stage fermentation can render the bioconversion of lignocellulose to ethanol more attractive due to increased final alcohol concentration. Journal of Industrial Microbiology & Biotechnology (2002) 29, 124–128 doi:10.1038/sj.jim.7000287 Received 20 February 2002/ Accepted in revised form 04 June 2002     

Itaconic acid production by immobilizedAspergillus terreus from xylose and glucose

Summary Aspergillus terreus NRRC 1960 spores were entrapped in calcium alginate gel beads or alternotely the fungal mycelium was immobilized either on Celite R-626 or in agar gel cubes, and the biocatalyst was employed both in repeated batch and in continuous column reactors to produce itaconic acid from D-xylose or D-glucose. The highest itaconic acid yield obtained in a submerged culture batch fermentation was 54.5% based on total initial glucose (55 g/l) with a volumetric productivity of 0.32 g/l h, and 44.8% from xylose (67 g/l) with a productivity of 0.20 g/l h. In a repeated batch fermentation mycelium immobilized in agar gel had a productivity of 0.112 g/l h, and mycelium grown from spores immobilized in calcium alginate gel 0.06 g/l h, both from xylose (60 g/l). With the best immobilized biocatalyst system used employing Celite R-626 as a carrier, volumetric productivities of 1.2 g/l h from glucose and 0.56 g/l h from xylose (both at 60 g/l) were obtained in continuous column operation for more than 2 weeks.     

聚氨酯固定化热带假丝酵母发酵木糖醇

固定在多孔聚氨酯载体中的热带假丝酵母(Candida tropicalis), 可有效地利用玉米芯半纤维素水解液生产木糖醇。在摇瓶条件下, 采用分批发酵方式, 确立了适宜的发酵工艺参数为: 接种量7%, 聚氨酯加入量1.0 g/100 mL, 温度30°C, 初始pH值6.0, 分段改变摇床转速进行溶氧调节, 其中0~24 h 为200 r/min; 24 h~46 h为140 r/min。聚氨酯固定化提高了菌体对发酵抑制物的耐受力, 固定化细胞密度高, 发酵性能稳定, 发酵产率和体积生产速率都有所提高。水解液未经脱色与离子交换便可转化成木糖醇, 大幅降低了成本, 显示了良好的应用前景。固定化细胞连续重复进行12批次21 d的发酵, 木糖醇得率平均为67.6%, 体积生产速率平均为1.92 g/(L·h)。     

Evaluation of continuous ethanol fermentation of dilute-acid corn stover hydrolysate using thermophilic anaerobic bacterium <Emphasis Type="Italic">Thermoanaerobacter</Emphasis> BG1L1

Dilute sulfuric acid pretreated corn stover is potential feedstock of industrial interest for second generation fuel ethanol production. However, the toxicity of corn stover hydrolysate (PCS) has been a challenge for fermentation by recombinant xylose fermenting organisms. In this work, the thermophilic anaerobic bacterial strain Thermoanaerobacter BG1L1 was assessed for its ability to ferment undetoxified PCS hydrolysate in a continuous immobilized reactor system at 70°C. The tested strain showed significant resistance to PCS, and substrate concentrations up to 15% total solids (TS) were fermented yielding ethanol of 0.39–0.42 g/g-sugars consumed. Xylose was nearly completely utilized (89–98%) for PCS up to 10% TS, whereas at 15% TS, xylose conversion was lowered to 67%. The reactor was operated continuously for 135 days, and no contamination was seen without the use of any agent for preventing bacterial infections. This study demonstrated that the use of immobilized thermophilic anaerobic bacteria for continuous ethanol fermentation could be promising in a commercial ethanol process in terms of system stability to process hardiness and reactor contamination. The tested microorganism has considerable potential to be a novel candidate for lignocellulose bioconversion into ethanol.     

Crabtree-negative characteristics of recombinant xylose-utilizing Saccharomyces cerevisiae

For recombinant xylose-utilizing Saccharomyces cerevisiae, ethanol yield and productivity is substantially lower on xylose than on glucose. In contrast to glucose, xylose is a novel substrate for S. cerevisiae and it is not known how this substrate is recognized on a molecular level. Failure to activate appropriate genes during xylose-utilization has the potential to result in sub-optimal metabolism and decreased substrate uptake. Certain differences in fermentative performance between the two substrates have thus been ascribed to variations in regulatory response. In this study differences in substrate utilization of glucose and xylose was analyzed in the recombinant S. cerevisiae strain TMB3400. Continuous cultures were performed with glucose and xylose under carbon- and nitrogen-limited conditions. Whereas biomass yield and substrate uptake rate were similar during carbon-limited conditions, the metabolic profile was highly substrate dependent under nitrogen-limited conditions. While glycerol production occurred in both cases, ethanol production was only observed for glucose cultures. Addition of acetate and 2-deoxyglucose pulses to a xylose-limited culture was able to stimulate transient overflow metabolism and ethanol production. Application of glucose pulses enhanced xylose uptake rate under restricted co-substrate concentrations. Results are discussed in relation to regulation of sugar metabolism in Crabtree-positive and -negative yeast.     

Ethanol production at 45°C by Kluyveromyces marxianus IMB3 immobilized in magnetically responsive alginate matrices

Summary The thermotolerant yeast, Kluyveromyces marxianus IMB3 produced 11g ethanol/l during growth at 45°C on media containing 4% (w/v) lactose when immobilized in alginate beads whereas the free cells produced 5g ethanol/l. A magnetically responsive biocatalyst, prepared by incorporating Fe₃O₄ into the alginate matrix increased ethanol production to 12g/l in batch-fed reactors. Ethanol concentrations were further increased to a maximum of 18g/l by immobilization of the endogenous K. marxianus -galactosidase to the Fe₃O₄ particles prior to inclusion into the alginate matrix. Maximum ethanol productivity by the system was 87% of the maximum theoretical yield.     

Fermentation of sugar cane bagasse hemicellulosic hydrolysate and sugar mixtures to ethanol by recombinant Escherichia coli KO11

Escherichia coli KO11, carrying the ethanol pathway genes pdc (pyruvate decarboxylase) and adh (alcohol dehydrogenase) from Zymomonas mobilis integrated into its chromosome, has the ability to metabolize pentoses and hexoses to ethanol, both in synthetic medium and in hemicellulosic hydrolysates. In the fermentation of sugar mixtures simulating hemicellulose hydrolysate sugar composition (10.0 g of glucose/l and 40.0 g of xylose/l) and supplemented with tryptone and yeast extract, recombinant bacteria produced 24.58 g of ethanol/l, equivalent to 96.4% of the maximum theoretical yield. Corn steep powder (CSP), a byproduct of the corn starch-processing industry, was used to replace tryptone and yeast extract. At a concentration of 12.5 g/l, it was able to support the fermentation of glucose (80.0 g/l) to ethanol, with both ethanol yield and volumetric productivity comparable to those obtained with fermentation media containing tryptone and yeast extract. Hemicellulose hydrolysate of sugar cane bagasse supplemented with tryptone and yeast extract was also readily fermented to ethanol within 48 h, and ethanol yield achieved 91.5% of the theoretical maximum conversion efficiency. However, fermentation of bagasse hydrolysate supplemented with 12.5 g of CSP/l took twice as long to complete. This revised version was published online in November 2006 with corrections to the Cover Date.     

An improvement in Pichia stipitis fermentation of acid-hydrolysed hemicellulose achieved by overliming (calcium hydroxide treatment) and strain adaptation

The fermentability of a corn cob, acid-hydrolysed hemicellulose by Pichia stipitis was considerably improved by pre-treatment with Ca(OH)₂. The total sugars utilized and ethanol yield for the untreated hydrolysate were 18% and 0.21 g/g, respectively, compared with 82% and 0.32 g/g respectively for the treated material. Adaptation of the yeast to the hydrolysate resulted in a significantly higher fermentation rate with over 90% of the initial total sugars being utilized and an ethanol yield and maximum ethanol concentration of 0.41 g/g and 13.3 g/l, respectively.The authors are with the USDA Forest Products Laboratory. One Gifford Pinchot Drive. Madison, WI, 53705 USA     

Adaptation of Candida shehatae and Pichia stipitis to wood hydrolysates for increased ethanol production

Summary Candida shehatae ATCC 22984 and Pichia stipitis CBS 5776 were tested for ethanol production from xylose, glucose-xylose mixtures, and aspen wood total hydrolysates. Adaptation of these yeasts to wood hydrolysate solutions by recycling resulted in improved substrate utilization and ethanol production. Compared to the non-adapted cultures, recycled C. shehatae and P. stipitis in aspen hydrolysate increased g ethanol/g sugar consumed from 0.39 and 0.41 to 0.45 and 0.47; while ethanol production from a 70:30 glucose-xylose solution (total sugars 140 g/L) was 45 g/L in 24 h and 60 g/L in 72 h with the adapted yeasts compared to 15 g/L and 28 g/L in the same times with the parent strains.     

Enhanced ethanol production from industrial lignocellulose hydrolysates by a hydrolysate-cofermenting Saccharomyces cerevisiae strain

Industrial production of lignocellulosic ethanol requires a microorganism utilizing both hexose and pentose, and tolerating inhibitors. In this study, a hydrolysate-cofermenting Saccharomyces cerevisiae strain was obtained through one step in vivo DNA assembly of pentose-metabolizing pathway genes, followed by consecutive adaptive evolution in pentose media containing acetic acid, and direct screening in biomass hydrolysate media. The strain was able to coferment glucose and xylose in synthetic media with the respective maximal specific rates of glucose and xylose consumption, and ethanol production of 3.47, 0.38 and 1.62 g/g DW/h, with an ethanol titre of 41.07 g/L and yield of 0.42 g/g. Industrial wheat straw hydrolysate fermentation resulted in maximal specific rates of glucose and xylose consumption, and ethanol production of 2.61, 0.54 and 1.38 g/g DW/h, respectively, with an ethanol titre of 54.11 g/L and yield of 0.44 g/g. These are among the best for wheat straw hydrolysate fermentation through separate hydrolysis and cofermentation.