Individual and combined effects of physicochemical parameters on ellagitannin acyl hydrolase and ellagic acid production from ellagitannin by <Emphasis Type="Italic">Aspergillus oryzae</Emphasis>

The individual and interactive effects of physicochemical parameters on ellagitannin acyl hydrolase activity and ellagic acid production by Aspergillus oryzae using ellagitannins from acorn fringe of oak as substrate were studied. Ellagitannins concentration, incubation time were identified as important physicochemical parameters influencing the enzyme synthesis and the production accumulation, and the substrate concentration with initial pH was determined to has an interactive effect on the enzyme synthesis, while ellagitannins concentration and initial pH with incubation time were found to have interactions on the production accumulation. Furthermore, the parameters were optimized by quadratic programming. Under optimum condition, the fermentation run lasted 84 h with 4 g L⁻¹ ellagitannins concentration, yielding 17.7% ellagic acid. However, the maximum enzyme activity was obtained in 96 h with 5 g L⁻¹ substrate concentration. The research demonstrated a possible way to develop an efficient approach for recovery of higher added-value product (ellagic acid) from forestry byproduct (acorn fringe of oak).     

Utilization of acorn fringe for ellagic acid production by Aspergillus oryzae and Endomyces fibuliger

Conversion of acorn fringe extract into ellagic acid production by Aspergillus oryzae and Endomyces fibuliger were investigated. The results showed that ellagic acid production was maximized when co-fermentation of the two fungi was performed at 30 degrees C and pH 5.0 with 5.7 g/l of initial substrate concentration, which were close to the optimal values for both fungi to yield an appropriate consortium of hydrolytic enzymes. Meanwhile, it was found that the co-fermentation could compensate the deficiencies in the level of polyphenol oxidase activity from pure A. oryzae and the levels of ellagitannin acyl hydrolase and beta-glucosidase activities from pure E. fibuliger, resulting in. 0.91 g/l of biomass concentration containing 1.84 g/l of ellagic acid. The research not only demonstrates that the co-fermentation is an effective approach to utilize forest byproduct for ellagic acid production, but also provides more evidences for understanding evolution of ellagic acid production with enzymes actions, which is important for process control of ellagic acid production in industrial application.     

Ellagic acid from acorn fringe by enzymatic hydrolysis and combined effects of operational variables and enzymes on yield of the production

The individual effects of three different enzyme types -- one single enzyme (ellagitannin acyl hydrolase) and two combinations of enzymes (ellagitannin acyl hydrolase-beta-glucosidase-polyphenol oxidase and ellagitannin acyl hydrolase-cellulase-xylanase) -- on ellagic acid yield, combined with other process parameters -- enzyme concentration, hydrolysis time, particle size and solid-to-liquid ratio -- were evaluated by response surface methodology. The selection of the enzymes for the study was based on preliminary experiments that showed higher increments in ellagic acid yield. The quantitative parameters studied were enzyme concentration (0.1, 0.45, 2 w/w or %), solid-to-liquid ratio (0.05, 0.15, 0.2), particle size (220, 445, 900 microm) and hydrolysis time (60, 89, 132 min). Experimental data for ellagic acid yield obtained with a single enzyme and two combination enzymes correlated very well with process parameters (P<0.0001), resulting in models with high coefficient of determination for ellagic acid yield (r(2)=0.9636). The combinations of enzymes appeared more effective for ellagic acid production than the single enzyme did. The yield of ellagic acid from non-heat-treated acorn fringe by the use of enzymes in general increased, compared with that from heat-treated material. The research opens a technological-efficient way and develop easily-available renewable raw material for ellagic acid production.     

里氏木霉与米根霉混合固态发酵产纤维素酶

以里氏木霉及米根霉单菌固态发酵为对象,考察不同混合发酵形式对里氏木霉与米根霉混合固态发酵产纤维素酶的影响。结果表明:同时接种里氏木霉与米根霉,试验考察的两菌种接种量比1∶1(以孢子个数计)及5∶1条件下,两菌未产生明显协同产酶作用。米根霉延时(24 h)接种且菌种量比5∶1以及米根霉延时(48 h)接种且菌种量比1∶1,2种发酵形式产酶情况类似,滤纸酶活(FPA)及羧甲基纤维素酶(CMCase)酶活相对米根霉单菌发酵有所提高,而β-葡萄糖苷酶(β-GA)酶活相对里氏木霉单菌固态发酵结束时分别增加4.66及4.40倍,可以发现两菌产生一定协同作用。在米根霉延时(48 h)接种且菌种量比5∶1的发酵形式下,FPA及CMCase在发酵第7天酶活分别达到44.04 IU/g、627.14 U/g(以1 g干曲计),分别是里氏木霉固态单菌发酵产酶达到稳定期时酶活的1.36和1.63倍,两菌产生了有效的协同作用。     

Optimization of Ellagitannase Production by Aspergillus niger GH1 by Solid-State Fermentation

Ellagic acid is one of the most bioactive antioxidants with important applications in pharmaceutical, cosmetic, and food industries. However, there are few biotechnological processes developed for its production, because it requires precursors (ellagitannins) and the corresponding biocatalyst (ellagitannase). The aim of this study was to optimize the culture conditions for ellagitannase production by Aspergillus niger in solid-state fermentation (SSF). The bioprocess was carried out into a column bioreactor packed with polyurethane foam impregnated with an ellagitannins solution as carbon source. Four strains of Aspergillus niger (PSH, GH1, HT4, and HC2) were evaluated for ellagitannase production. The study was performed in two experimental steps. A Plackett–Burman design was used to determine the influencing parameters on ellagitannase production. Ellagitannins concentration, KCl, and MgSO₄ were determined to be the most significant parameters. Box–Behnken design was used to define the interaction of the selected parameters. The highest enzyme value was obtained by A. niger PSH at concentrations of 7.5 g/L ellagitannins, 3.04 g/L KCl, and 0.76 g/L MgSO₄. The methodology followed here allowed increasing the ellagitannase activity 10 times over other researcher results (938.8 U/g ellagitannins). These results are significantly higher than those reported previously and represent an important contribution for the establishment of a new bioprocess for ellagic acid and ellagitannase production.     

里氏木霉产纤维素酶研究进展

木质纤维素类生物质被认为是重要且可持续的可再生能源,其主要组成部分是纤维素.纤维素酶是一种能将纤维素分解为葡萄糖的复合酶,能有效地降解木质纤维素生物质.真菌、细菌、放线菌、酵母等多种微生物均可以产生纤维素酶,其中里氏木霉具有完整的纤维素酶系结构,常作为生物技术领域中一个重要菌株,广泛应用于纤维素酶的商业生产.介绍了纤维...     

Citric acid production by a novel Aspergillus niger isolate: II. Optimization of process parameters through statistical experimental designs

In this work, sequential optimization strategy, based on statistical designs, was employed to enhance the production of citric acid in submerged culture. For screening of fermentation medium composition significantly influencing citric acid production, the two-level Plackett-Burman design was used. Under our experimental conditions, beet molasses and corn steep liquor were found to be the major factors of the acid production. A near optimum medium formulation was obtained using this method with increased citric acid yield by five-folds. Response surface methodology (RSM) was adopted to acquire the best process conditions. In this respect, the three-level Box-Behnken design was applied. A polynomial model was created to correlate the relationship between the three variables (beet molasses, corn steep liquor and inoculum concentration) and citric acid yield. Estimated optimum composition for the production of citric acid is as follows pretreated beet molasses, 240.1g/l; corn steep liquor, 10.5g/l; and spores concentration, 10(8)spores/ml. The optimum citric acid yield was 87.81% which is 14 times than the basal medium. The five level central composite design was used for outlining the optimum values of the fermentation factors initial pH, aeration rate and temperature on citric acid production. Estimated optimum values for the production of citric acid are as follows initial pH 4.0; aeration rate, 6500ml/min and fermentation temperature, 31.5 degrees C.     

Development of a low pH fermentation strategy for fumaric acid production by Rhizopus oryzae

Dicarboxylic acids that are produced from renewable resources are becoming attractive building blocks for the polymers industry. In this respect, fumaric acid is very interesting. Its low aqueous solubility facilitates product recovery. To avoid excessive waste salt production during downstream processing, a low pH for fumaric acid fermentation will be beneficial. Studying the influence of pH, working volume and shaking frequency on cell cultivation helped us to identify the best conditions to obtain appropriate pellet morphologies of a wild type strain of Rhizopus oryzae. Using these pellets, the effects of pH and CO(2) addition were studied to determine the best conditions to produce fumaric acid in batch fermentations under nitrogen-limited conditions with glucose as carbon source. Decreasing either the fermentation pH below 5 or increasing the CO(2) content of the inlet air above 10% was unfavourable for the cell-specific productivity, fumaric acid yield, and fumaric acid titer. However, switching off the pH control late in the batch phase did not affect these performance parameters and allowed achieving pH of 3.6. A concentration of 20 gL(-1) of fumaric acid was obtained at pH 3.6 while the average cell mass specific productivity and fumaric acid yield were the same as at pH 5.0. Consequently, relatively modest amounts of inorganic base were required for pH control, while recovery of the acid should be relatively easy at pH 3.6.     

Production of L(+)-lactic acid from glucose and starch by immobilized cells of Rhizopus oryzae in a rotating fibrous bed bioreactor

A rotating fibrous-bed bioreactor (RFB) was developed for fermentation to produce L(+)-lactic acid from glucose and cornstarch by Rhizopus oryzae. Fungal mycelia were immobilized on cotton cloth in the RFB for a prolonged period to study the fermentation kinetics and process stability. The pH and dissolved oxygen concentration (DO) were found to have significant effects on lactic acid productivity and yield, with pH 6 and 90% DO being the optimal conditions. A high lactic acid yield of 90% (w/w) and productivity of 2.5 g/L.h (467 g/h.m(2)) was obtained from glucose in fed-batch fermentation. When cornstarch was used as the substrate, the lactic acid yield was close to 100% (w/w) and the productivity was 1.65 g/L.h (300 g/h.m(2)). The highest concentration of lactic acid achieved in these fed-batch fermentations was 127 g/L. The immobilized-cells fermentation in the RFB gave a virtually cell-free fermentation broth and provided many advantages over conventional fermentation processes, especially those with freely suspended fungal cells. Without immobilization with the cotton cloth, mycelia grew everywhere in the fermentor and caused serious problems in reactor control and operation and consequently the fermentation was poor in lactic acid production. Oxygen transfer in the RFB was also studied and the volumetric oxygen transfer coefficients under various aeration and agitation conditions were determined and then used to estimate the oxygen transfer rate and uptake rate during the fermentation. The results showed that the oxygen uptake rate increased with increasing DO, indicating that oxygen transfer was limited by the diffusion inside the mycelial layer.     

Microbial production of ellagic acid and biodegradation of ellagitannins

In the last years, tannin biodegradation has been the subject of a lot of studies due to its commercial importance and scientific relevance. Tannins are molecules of low biodegradation and represent the main chemical group of natural anti-microbials occurring in the plants. Among the different kinds of tannins, ellagitannins represent the group less studied manly due to their diversity and chemical complexity. The general outline of this work includes information on tannins, their classification and properties, biodegradation, ellagic acid production, and potential applications. In addition, it describes molecular, catalytic, and functional information. Special attention has been focused on the biodegradation of ellagitannins describing the possible role of microbial enzymes in the production of ellagic acid.     

Continuous production of ellagic acid in a packed-bed reactor

Ellagic acid is a high-value bioactive compound that is used in the food, cosmetic and pharmaceutical industries. The aim of this work was to develop a continuous system for ellagic acid production. Ellagitannase produced by solid-state fermentation and attached to polyurethane foam particles was used as a biocatalyst in a continuous bioreactor for the hydrolysis of ellagitannins from pomegranate by-product. A packed-bed reactor containing the biocatalyst (22.22 Units per gram of dry solid, U gds⁻¹) was fed with a pomegranate ellagitannins solution (0.1%, w/v) at a flow rate of 0.27 mL min⁻¹ at 60 °C. The bioreactor completed several biotransformations while maintaining the hydrolysis rate (60%) with a half-life of 10 continuous cycles of ellagic acid production. Volumetric productivity and ellagic acid yield were 1.09 g L⁻¹ h⁻¹ and 235.89 mg g⁻¹ of pomegranate ellagitannins during the first 70 min of hydrolysis, respectively. The developed biocatalyst showed good operational and mechanical stability and may be successfully used for ellagitannin hydrolysis in a continuous system. This is the first report of high-yield continuous production of ellagic acid using an auto-immobilized enzyme.     

茴香酸产生菌发酵条件的优化

为提高微生物降解反式茴脑获得茴香酸的产量,对假单胞菌Pseudomonas sp.NT2的发酵参数进行优化,以提高降解过程的转化率。利用单因素试验考察碳氮源种类及浓度、反式茴脑添加量、发酵温度、接种量、初始pH以及装液量对茴香酸生成量、反式茴脑降解率的影响,通过Plackett-Burman试验和最陡爬坡试验确定影响茴香酸生成量的显著因素并获取中心点,最后采用Box-Behnken模型进行响应面优化得到最佳发酵条件并验证。结果表明氯化铵浓度、初始pH和装液量是显著影响因素,最佳发酵条件为:柠檬酸钠10 g/L,氯化铵1.26 g/L,反式茴脑添加量1%,发酵温度30℃,接种量4%,初始pH 7.9,装液量42 mL/250 mL。优化后茴香酸生成量为7.24 g/L,为优化前的3.5倍,茴香酸摩尔生成率为80.72%,反式茴脑降解率为89.81%,分别比优化前提高了270.28%和97.78%。综上,假单胞菌NT2是生物转化生产茴香酸的潜力菌株。响应面优化可以显著提高反式茴脑的降解率和茴香酸产量,这为大规模生产茴香酸奠定了基础。     

Optimization of ellagic acid accumulation by Aspergillus niger GH1 in solid state culture using pomegranate shell powder as a support

This report describes an investigation of ellagic acid accumulation (EAA) in solid state culture (SSC) using Aspergillus niger GH1 and powdered pomegranate peel as a support. Various culture conditions (temperature, initial moisture, levels of inoculum and concentration of salts) were evaluated using a Plackett–Burman design (PBD) for screening culture factors followed by a central composite design (CCD) for enhancing the EAA. Temperature, MgSO₄ and KCl concentration were identified as significant parameters for EAA in SSC. This enhancement procedure resulted in 15.5-fold increase in EAA (8.48–132.62 mg/g) when the selected culture conditions were evaluated in a kinetic study of biodegradation of ellagitannins to produce ellagic acid. This work proposes a biotechnological alternative to obtain a highly valuable, high-quality compound from agro-industrial wastes through SSC.     

Evaluation of culture conditions for cellulase production by two Trichoderma reesei mutants under solid-state fermentation conditions

Response surface methodology (RSM) was used to evaluate the effects of fermentation parameters for cellulase production by Trichoderma reesei QM9414 and T. reesei MCG77 in solid-state fermentation using rice bran as substrate. Initial pH, moisture content and temperature were optimized using filter paper activity (FPA) as response. Statistical analysis of the results for T. reesei QM9414 showed that only moisture content had significant effect on cellulase activity and had a linear effect on enzyme activity (maximum enzyme activities were obtained at 70% moisture content). The results for T. reesei MCG77 showed that temperature and moisture content were the most significant parameters for cellulase activity. The optimum cellulase production was in the temperature range of 25-30 degrees C and moisture content between 55% and 70%. After the optimization, the FPA in T. reesei MCG77 was increased by 2.5 folds compared to that of T. reesei QM9414.     

Selection of thermotolerant yeast strains for simultaneous saccharification and fermentation of cellulose

A total of 58 yeast strains from 12 genera were assayed for their ability to grow and ferment carbohydrates in standard Durham tube test at 40, 43, and 46 degrees C. Based on the kinetic parameters for glucose fermentation in shaken flask cultures, the strain Fabospora fragilis CCY51-1-1 was chosen for further studies. It reached about 56.0 and 35.0 g ethanol/L from approximately 140 g glucose/L at 43 and 46 degrees C in less than 48 h, respectively. Trichoderma reesei cellulase preparation (400 FPU/L) had not distinct effect on the ethanol yield and biomass production by the selected strain in the first 12 h fermentation at 46 degrees C. Later a negligible decrease in both yields was observed. It was found that Fabospora fragilis did not grow or produce ethanol at 46 degrees C as tho initial ethanol concentration overcame 40 g/L.     

Direct fermentation of potato starch wastewater to lactic acid by Rhizopus oryzae and Rhizopus arrhizus

The biochemical kinetic of direct fermentation for lactic acid production by fungal species of Rhizopus arrhizus 3,6017 and Rhizopus oryzae 2,062 was studied with respect to growth pH, temperature and substrate. The direct fermentation was characterized by starch hydrolysis, accumulation of reducing sugar, and production of lactic acid and fungal biomass. Starch hydrolysis, reducing sugar accumulation, biomass formation and lactic acid production were affected with the variations in pH, temperature, and starch source and concentration. A growth condition with starch concentration approximately 20 g/l at pH 6.0 and 30°C was favourable for both starch saccharification and lactic acid fermentation, resulting in lactic acid yield of 0.87–0.97 g/g starch associated with 1.5–2.0 g/l fungal biomass produced in 36 h fermentation. R. arrhizus 3,6017 had a higher capacity to produce lactic acid, while R. oryzae 2,062 produced more fungal biomass under similar conditions.     

Production of β-1,3-glucanase from Trichoderma harzianum in surface and submerged culture processes and its role on protoplast generation from Trichoderma reesei mycelium

Surface and submerged culture studies were carried out for the production of extracellular -1,3-glucanase and carboxymethylcellulase from Trichoderma harzianum, NCIM 1185. The different parameters which influence the enzyme production, viz., spore age in the slant growth, seed age, and pH (initial) of the production medium have been optimized. The ranges of these parameters studied were: Spore age of T. harzianum between 2 and 10 days, seed age between 12 h and 48 h, and pH (initial) between 3 and 7. The other conditions of fermentation were: Temperature 30°C, gyratory shaker speed 160 rev. min^–1. It was observed that the activities of -1,3-glucanase and carboxymethylcellulase varied during the entire fermentation cycle which had a distinct effect on protoplast generation from T. reesei mycelium. The optimum values of the above-mentioned parameters for lytic enzymes production were: Spore age of T. harzianum in the slant growth 5 days, seed age 36 h, and pH (initial) 5.0 for both surface and submerged culture processes.Mr. S. Venkatesan, Department of Chemical Engineering, is thanked for his excellent secretarial help.     

L-苹果酸产生菌F-871变株合成延胡索酸酶的研究*

温特曲霉AspergilluswentiiF-871是高效转化延胡索酸为L-苹果酸的变株,通过对其合成延胡索酸酶的因素进行研究,筛选了培养基主要营养元素有L-精氨酸、酪氨酸、丝氨酸、天冬氨酸、苏氨酸、赖氨酸及相应含量丰富的酵母粉、黄豆饼粉和玉米浆。该变株生长阶段条件为:pH6.0,温度2830℃,培养时间为24h,酶合成阶段最适条件:接种量15%,初始pH6.8,培养温度2830℃,装量8090ml/500ml,酶合成周期40h。在优化的培养条件下,F-871变株延胡索酸酶合成水平可达156.33u/g,100ml发酵液中的酶可将延胡索酸转化为L-苹果酸32.06g,比国内一步发酵法产酸88.5%提高约4倍,转化率由85%提高到106.87%,发酵周期由90h缩短至57h。     

L-苹果酸产生菌F-871变株合成延胡索酸酶的研究

温特曲霉AspergilluswentiiF-871是高效转化延胡索酸为L-苹果酸的变株,通过对其合成延胡索酸酶的因素进行研究,筛选了培养基主要营养元素有L-精氨酸、酪氨酸、丝氨酸、天冬氨酸、苏氨酸、赖氨酸及相应含量丰富的酵母粉、黄豆饼粉和玉米浆。该变株生长阶段条件为:pH6.0,温度2830℃,培养时间为24h,酶合成阶段最适条件:接种量15%,初始pH6.8,培养温度2830℃,装量8090ml/500ml,酶合成周期40h。在优化的培养条件下,F-871变株延胡索酸酶合成水平可达156.33u/g,100ml发酵液中的酶可将延胡索酸转化为L-苹果酸32.06g,比国内一步发酵法产酸88.5%提高约4倍,转化率由85%提高到106.87%,发酵周期由90h缩短至57h。     

Effect of ellagitannin acyl hydrolase,xylanase and cellulase on ellagic acid production from cups extract of valonia acorns

Ellagic acid production from cups extract of valonia acorns by pure and mixed cultures of Aspergillus oryzae and Trichoderma reesei was investigated. Ellagitannin acyl hydrolase and xylanase as well as cellulase during the pure and mixed cultures were also determined. The results revealed that mixed culture could produce higher ellagic acid yield (23%) than either of pure culture. And it was found that the three enzymes from mixed culture appeared synergistic effect on ellagic acid production. Statistical analysis showed that ellagic acid yield was correlated very well with the three enzymes activities, resulting in the model for ellagic acid production with high R² value of 0.998 and significant level p < 0.004.