Influence of Medium Composition on Xylitol Bioproduction from Wheat Straw Hemicellulosic Hydrolysate

Summary Xylose-to-xylitol batch bioconversions from wheat straw hemicellulosic hydrolysate were carried out in Erlenmeyer flasks in order to assess the influence of medium composition (hydrolysate concentration, supplementation with ammonium sulphate, calcium chloride and rice bran extract, and initial pH) on xylitol production, productivity and yield. By using the screening design and the response surface methodologies, the statistically significant variables influencing the bioconversion were selected and linear models were fitted to the experimental data. According to the results, the best conditions to perform the bioconversion consisted in using a threefold concentrated hydrolysate supplemented with ammonium sulphate (1.0 g/l) and rice bran extract (5.0 g/l), whose pH was adjusted to 6.0 prior to inoculation. Under these conditions, a xylitol production of 24.17 g/l was observed after 72 h of fermentation, resulting in a productivity of 0.34 g/l h and in a bioconversion yield of 0.49 g/g.     

Fermentative production of dl-lactic acid from amylase-treated rice and wheat brans hydrolyzate by a novel lactic acid bacterium, Lactobacillus sp.

Rice and wheat brans, without additional nutrients and hydrolyzed by alpha-amylase and amyloglucosidase, were fermented to DL-lactic acid using a newly isolated strain of Lactobacillus sp. RKY2. In batch fermentations at 36 degrees C and pH 6, the amount of lactic acid in fermentation broth reached 129 g l(-1) by supplementation of rice bran with whole rice flour. The maximum productivity was 3.1 g lactic acid l(-1) h(-1) in rice bran medium supplemented with whole rice flour or whole wheat flour.     

Utilization of rice bran as nutrient source for fermentative lactic acid production

To reduce nutrient cost for lactic acid production, rice bran, one of agricultural wastes, was chosen as a nutrient source in this study. Although rice bran is rich in protein and vitamins, the use of rice bran without any treatment was inefficient in lactic acid production. Rice bran was treated by acid-hydrolysis before it was put in experiment, when it was hydrolyzed at initial pH 1, 30 g/L rice bran could provide a productivity to that degree of about 8 g/L YE, showing such a desirable result that the use of rice bran as nutrient source would be a solution for reducing nutrient cost. However, the addition of hydrolyzed rice bran prolonged lag phase of fermentation, especially, in the fermentation with rice bran hydrolyzed at initial pH 0.5, a prolonged lag phase of about 40 h was observed. According to the quantitative determination of thiamine, pyridoxine, organic nitrogen and carbon, the prolongation of lag phase might be the result from the destruction of B vitamins and excessive hydrolysis of protein. To shorten the lag phase, combining hydrolyzed rice bran with yeast extract (YE) of small amount was considered to be a solution. When 3g/L YE was combined with 30 g/L rice bran hydrolyzed at initial pH 1, obtained was a productivity 1.6 times higher than that of the control fermentation with 15 g/L YE.     

Lantana camara for fuel ethanol production using thermotolerant yeast

AIM: Evaluation of Lantana camara's use as feedstock for fuel ethanol production. METHODS AND RESULTS: Lantana camara plant material was hydrolysed with 1% sulfuric acid for 18 h at room temperature, followed by heat treatment of 121 degrees C for 20 min. Hemicellulosic hydrolyzate was separated and used for detoxification by ethyl acetate and overliming. Cellulosic fraction was hydrolysed with Aspergillus niger crude cellulase enzyme for 18 h at 55 degrees C. Using 15% (dw/v) substrate 73 g l(-1) total reducing sugars were obtained to give 78.7% hydrolysis of carbohydrate content. Acid and enzyme hydrolyzates were mixed equally and used for fermentation with thermotolerant Saccharomyces cerevisiae (VS(3)). Yeast fermented L. camara hydrolyzate well with a fermentation efficiency of 83.7% to give an ethanol yield of 0.431 +/- 0.018 g ethanol pre g sugar and productivity of 0.5 +/- 0.021 g l(-1) h(-1). CONCLUSIONS: Even though inhibitors were present in L. camara hydrolyzate, maximum sugars were utilized by thermotolerant yeast. SIGNIFICANCE AND IMPACT OF THE STUDY: Use of L. camara for fuel ethanol production with improved strains and detoxification can be recommended.     

Dilute acid pretreatment, enzymatic saccharification, and fermentation of rice hulls to ethanol

Rice hulls, a complex lignocellulosic material with high lignin (15.38 +/- 0.2%) and ash (18.71 +/- 0.01%) content, contain 35.62 +/- 0.12% cellulose and 11.96 +/- 0.73% hemicellulose and has the potential to serve as a low-cost feedstock for production of ethanol. Dilute H2SO4 pretreatments at varied temperature (120-190 degrees C) and enzymatic saccharification (45 degrees C, pH 5.0) were evaluated for conversion of rice hull cellulose and hemicellulose to monomeric sugars. The maximum yield of monomeric sugars from rice hulls (15%, w/v) by dilute H2SO4 (1.0%, v/v) pretreatment and enzymatic saccharification (45 degrees C, pH 5.0, 72 h) using cellulase, beta-glucosidase, xylanase, esterase, and Tween 20 was 287 +/- 3 mg/g (60% yield based on total carbohydrate content). Under this condition, no furfural and hydroxymethyl furfural were produced. The yield of ethanol per L by the mixed sugar utilizing recombinant Escherichia colistrain FBR 5 from rice hull hydrolyzate containing 43.6 +/- 3.0 g fermentable sugars (glucose, 18.2 +/- 1.4 g; xylose, 21.4 +/- 1.1 g; arabinose, 2.4 +/- 0.3 g; galactose, 1.6 +/- 0.2 g) was 18.7 +/- 0.6 g (0.43 +/- 0.02 g/g sugars obtained; 0.13 +/- 0.01 g/g rice hulls) at pH 6.5 and 35 degrees C. Detoxification of the acid- and enzyme-treated rice hull hydrolyzate by overliming (pH 10.5, 90 degrees C, 30 min) reduced the time required for maximum ethanol production (17 +/- 0.2 g from 42.0 +/- 0.7 g sugars per L) by the E. coli strain from 64 to 39 h in the case of separate hydrolysis and fermentation and increased the maximum ethanol yield (per L) from 7.1 +/- 2.3 g in 140 h to 9.1 +/- 0.7 g in 112 h in the case of simultaneous saccharification and fermentation.     

绿色木霉ZY-1固态发酵产纤维素酶

利用筛选的绿色木霉ZY-1（Trichoderma viride ZY-1）固态发酵产纤维素酶,采用稻草和麸皮为底物,考察稻草与麸皮比例随发酵时间对产酶的影响。结果表明：底物中,在m（稻草）：m（麸皮）为0：5和1：4时,发酵48h,pH保持4．5左右,还原糖量急剧上升,胞外蛋白产量最低;仅以稻草作底物时,整个发酵过程中pH约为7,还原糖量最低,胞外蛋白产量较高而滤纸酶活、羧甲基纤维素酶（CMCase）和β-葡萄糖苷酶（β-Gase）酶活均较低;在m（稻草）：m（麸皮）为3：2时,发酵96h,滤纸酶活达最大值5．01U／g干曲;m（稻草）：m（麸皮）为1：4时,发酵96h,β-Gase酶活达最大值4．6U／g干曲;m（稻草）：m（麸皮）为4：1时,发酵72h,CMCase酶活达最大值6．01U／g干曲。因此,底物中存在适量的稻草和麸皮有利于Trichoderma viride ZY—1产纤维素酶。     

Biotechnological production of l(+)-lactic acid from wood hydrolyzate by batch fermentation of Enterococcus faecalis

The inhibition of lactic acid fermentation by wood hydrolyzate was decreased (approx. 20%) by adaptation of Enterococcus faecalis RKY1 to wood hydrolyzate-based medium whereby lactic acid productivity and cell growth were enhanced by 0.5 g l(-1) h(-1) and 2.1 g l(-1), respectively. When the diluted or concentrated wood hydrolyzate (equivalent to 25-100 g glucose l(-1)) was supplemented with 15 g yeast extract l(-1), 24-93 g lactic acid l(-1) was produced at a rate between 1.7 g l(-1) h(-1) and 3.2 g l(-1) h(-1).     

Study of restrictase Sal GI biosynthesis and optimum conditions for its isolation

The effect of the growing phase of Streptomyces albus G. and the components of the culture medium on the biosynthesis of restriction endonuclease Sal GI was studied. The conditions of DNA sedimentation with streptomycin sulfate and polyethylenimine and separation of proteins with ammonium sulfate were investigated as well. A maximal quantity of the enzyme was observed in the cells in 18-20 h of cultivation in flasks on a shaker. The optimal concentrations of the medium components (g/l) were found by mathematical methods of the experiment planning: glucose--19,0; pepton--5.2; K2HPO4 X 3H2O - 5.0. The optimal concentrations for DNA sedimentation with streptomycin sulfate and polyethylenimine were found to be 1.8-2.0% and 0.2-0.3%, respectively. The optimal concentration of ammonium sulfate for protein separation is 70% of saturation.     

Production of lactic acid and fungal biomass by Rhizopus fungi from food processing waste streams

This study proposed a novel waste utilization bioprocess for production of lactic acid and fungal biomass from waste streams by fungal species of Rhizopus arrhizus 36017 and R. oryzae 2062. The lactic acid and fungal biomass were produced in a single-stage simultaneous saccharification and fermentation process using potato, corn, wheat and pineapple waste streams as production media. R. arrhizus 36017 gave a high lactic acid yield up to 0.94-0.97 g/g of starch or sugars associated with 4-5 g/l of fungal biomass produced, while 17-19 g/l fungal biomass with a lactic acid yield of 0.65-0.76 g/g was produced by the R. oryzae 2062 in 36-48 h fermentation. Supplementation of 2 g/l of ammonium sulfate, yeast extract and peptone stimulated an increase in 8-15% lactic acid yield and 10-20% fungal biomass.     

饲料营养成分对草鱼,团头鲂和青鱼鱼种阶段的饲料可消化能值的影响

为了探讨饲料可消化能值同饲料营养成分之间的关系,用Ｃｒ２Ｏ３作指示物,分别测定了鱼粉和大豆粕等饲料原料的草鱼（Ｃｔｅｎｏｐｈａｒｙｎｇｏｄｏｎ　ｉｄｅｌｌａ）团头鲂（Ｍｅｇａｌｏｂｒａｍａ ａｍｂｌｙｏｃｅｐｈａｌａ　Ｙｉｈ）青鱼（Ｍｙｌｏｐａｒｙｎｇｏｄｏｎ　ｐｉｃｅｕｓ）鱼种饲料的可消化能,用微机计算分析测试结果,发现饲料可消化能值随饲料蛋白质和／或脂肪食量增加而增加;随饲料无氮浸出物和／或纤维含量增加而降低。同时,“优选”出了有一定实用价值的估算草鱼、团头鲂和青鱼鱼种饲料可消化能值的回归方程。     

An economical approach for d-lactic acid production utilizing unpolished rice from aging paddy as major nutrient source

In order to reduce the raw material cost of d-lactic acid fermentation, the unpolished rice from aging paddy was used as major nutrient source in this study. The unpolished rice saccharificate, wheat bran powder and yeast extract were employed as carbon source, nitrogen source and growth factors, respectively. Response surface methodology (RSM) was applied to optimize the dosages of medium compositions. As a result, when the fermentation was carried out under the optimal conditions for wheat bran powder (29.10 g/l) and yeast extract (2.50 g/l), the d-lactic acid yield reached 731.50 g/kg unpolished rice with a volumetric production rate of 1.50 g/(l h). In comparison with fresh corn and polished rice, the d-lactic acid yield increased by 5.79% and 8.71%, and the raw material cost decreased by 65% and 52%, respectively, when the unpolished rice was used as a major nutrient source. These results might provide a reference for the industrial production of d-lactic acid.     

Influence of media composition on xylitol fermentation by Candida guiliiermondii using response surface methodology

Summary The bioconversion of xylose to xylitol by the yeast Candida guilliermondii FTI 20037 was evaluated under different nutritional conditions using rice straw hemicellulose hydrolysate. Statistical designs were used to determine the fermentation medium composition. Ammonium sulfate and rice bran have been identified as required nutrients in the hydrolysate since there was a significant interaction between them. In the presence of both nutrients, the xylitol yield factor (Yp/s) and volumetric productivities (Qp) were 0.68 g/g and 0.54 g/L.h, respectively.     

The effect of whey protein hydrolyzates on the lactic acid fermentation

Summary The batch fermentation of whey permeate to lactic acid was improved markedly by the addition of enzymehydrolyzed whey protein. Acid concentrations greater than 90 g/l were achieved at a productivity of 4.3 g/l per h and a 98% substrate use. Cell mass concentration reached 6 g/l. The acid productivity achieved is somewhat higher than that typical for fermentation of whole whey. The process economics, based on in-house hydrolyzate preparation, look promising. Presented in this paper are the experimental results showing the effects of hydrolyzate concentration on acid and cell mass production.     

Optimization of the pretreatment of rice straw hemicellulosic hydrolyzates for microbial production of xylitol

Hemicellulosic hydrolyzate obtained from rice straw was evaluated to determine if it was a suitable fementation medium for the production of xylitol byCandida mogii ATCC 18364. To obtain xylose selectively from rice straw, it is important to establish rapid hydrolysis conditions that yield xylose-rich substrates. The results of hydrolysis experiments indicated that the optimal reaction conditions for the recovery of xylose from rice straw hemicellulose were obtained using a sulfuric acid concentration of 1.5%, a reaction temperature of 130°C, a reaction time of 20 min and a solid to liquid ratio of 1∶10. Because the fermentation of concentrated acid hydrolyzates can be inhibited by compounds present in the raw material or produced during the hydrolysis process, various methods were tested to determine if they could detoxify the hydrolyzates and thus improve xylitol production. The greatest xylitol yield (0.53 g/g) and volumetric productivity (0.38 g/L·h) were obtained when an overlimed hydrolyzate was treated with activated charcoal.     

Enhanced production of a thermostable xylanase from Streptomyces sp. QG-11-3 and its application in biobleaching of eucalyptus kraft pulp

A thermostable and cellulase-free xylanase has been produced from Streptomyces sp. QG-11-3 in solid substrate fermentation using wheat bran and eucalyptus kraft pulp as the prime solid substrates. The maximum xylanase yield obtained using these two substrates were 2360 U/g and 1200 U/g dry solid substrate at substrate:moisture ratios of 1:3 and 1:2.5, respectively. In immobilized cell system using polyurethane foam (PUF) and three nonwoven fabrics, namely, polyester, silk, and cotton, the xylanase yields were enhanced by 2.5-fold (203 U/ml), 1.91-fold (155 U/ml), 1.54-fold (125 U/ml), and 1.47-fold (119 U/ml), respectively, compared to the xylanase yield in liquid-batch fermentation (81 U/ml). In the biobleaching experiments, the xylanase dose of 3.5 U/g moisture free pulp exhibited the optimum bleach boosting of eucalyptus kraft pulp at pH 8.5 and 50 degrees C after 2 h of treatment. When xylanase treated pulp was subsequently treated with 4.5% chlorine, it resulted in reduction of kappa number by 25%, enhanced the brightness (%ISO) by 20% and improved the pulp properties such as tensile strength and burst factor by up to 63% and 8%, respectively.     

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     

Changes in lipid, fatty acids and phospholipids composition of whole rice bran after solid-state fungal fermentation

The aim of this study was to evaluate fermented rice bran phospholipids, lipids and fatty acid content in a fermentation solid system with Rhizopus oryzae fungus. For this, aliquots were withdrawn every 24h over 120 h. The content of phospholipids was determined by colorimetric method. Esterified fatty acids were separated by gas chromatography, then identified and quantified. The total lipids from fermented rice bran (FB) decreased from 20.4% to 11.2% in the range between 0 h and 120 h of fermentation while phospholipid contents were increased up to 2.4 mg P g(lipid)(-1). In fermented bran, oleic, palmitic and linoleic acids prevailed, with a decrease in saturated fatty acids (20%) and increase in the unsaturated ones (5%). This study showed that rice bran fermentation with R. oryzae can be applied to the production of phospholipids altering the saturated to unsaturated fatty acid ratio.     

Dilute acid pretreatment, enzymatic saccharification and fermentation of wheat straw to ethanol

Wheat straw consists of 48.57 ± 0.30% cellulose and 27.70 ± 0.12% hemicellulose on dry solid (DS) basis and has the potential to serve as a low cost feedstock for production of ethanol. Dilute acid pretreatment at varied temperature and enzymatic saccharification were evaluated for conversion of wheat straw cellulose and hemicellulose to monomeric sugars. The maximum yield of monomeric sugars from wheat straw (7.83%, w/v, DS) by dilute H₂SO₄ (0.75%, v/v) pretreatment and enzymatic saccharification (45 °C, pH 5.0, 72 h) using cellulase, β-glucosidase, xylanase and esterase was 565 ± 10 mg/g. Under this condition, no measurable quantities of furfural and hydroxymethyl furfural were produced. The yield of ethanol (per litre) from acid pretreated enzyme saccharified wheat straw (78.3 g) hydrolyzate by recombinant Escherichia coli strain FBR5 was 19 ± 1 g with a yield of 0.24 g/g DS. Detoxification of the acid and enzyme treated wheat straw hydrolyzate by overliming reduced the fermentation time from 118 to 39 h in the case of separate hydrolysis and fermentation (35 °C, pH 6.5), and increased the ethanol yield from 13 ± 2 to 17 ± 0 g/l and decreased the fermentation time from 136 to 112 h in the case of simultaneous saccharification and fermentation (35 °C, pH 6.0).     

响应曲面法优化灵芝廉价型深层发酵培养基的研究

为了获得生产用廉价型灵芝发酵培养基,采用中心组合旋转设计法和响应曲面法对低成本培养基组分进行了优化。优化的四个组分为玉米粉(x1)、麸皮粉(x2)、豆饼粉(x3)和蔗糖(x4)。结果表明,灵芝菌体发酵和多糖发酵的培养基预测模型分别为:Y1=15.1–0.31x1–0.34x2+0.36x3–0.44x4–1.26x12–1.98x22–0.85x32–1.15x42–0.59x2x3和Y2=2.0–0.08x1–0.08x2+0.04x3–0.09x4–1.13x12–0.33x22–0.08x32–0.16x42–0.16x2x3–0.10x1x4。从中获得菌体发酵的最优配方为:玉米粉19.7g/L,麸皮粉11.3g/L,豆饼粉6.3g/L,蔗糖19.5g/L;多糖发酵的最优配方为:玉米粉19.6g/L,麸皮粉11.0g/L,豆饼粉6.7g/L,蔗糖19.1g/L。150L发酵罐中试放大结果表明,灵芝菌体的产量为16.92g/L,多糖产量为1.86g/L。所得培养基为灵芝产品的高效低成本生产提供了基础。     

A comparison of liquid hot water and steam pretreatments of sugar cane bagasse for bioconversion to ethanol.

Sugar cane bagasse was pretreated with either liquid hot water (LHW) or steam using the same 25 l reactor. Solids concentration ranged from 1% to 8% for LHW pretreatment and was > or = 50% for steam pretreatment. Reaction temperature and time ranged from 170 to 230 degrees C and 1 to 46 min, respectively. Key performance metrics included fiber reactivity, xylan recovery, and the extent to which pretreatment hydrolyzate inhibited glucose fermentation. In four cases, LHW pretreatment achieved > or = 80% conversion by simultaneous saccharification and fermentation (SSF). > or = 80% xylan recovery, and no hydrolyzate inhibition of glucose fermentation yield. Combined effectiveness was not as good for steam pretreatment due to low xylan recovery. SSF conversion increased and xylan recovery decreased as xylan dissolution increased for both modes. SSF conversion, xylan dissolution. hydrolyzate furfural concentration, and hydrolyzate inhibition increased, while xylan recovery and hydrolyzate pH decreased, as a function of increasing LHW pretreatment solids concentration (1-8%). These results are consistent with the notion that autohydrolysis plays an important. if not exclusive, role in batch hydrothermal pretreatment. Achieving concurrently high (greater than 90%) SSF conversion and xylan recovery will likely require a modified reactor configuration (e.g. continuous percolation or base addition) that better preserves dissolved xylan.