Influence of solid substrate fermentation on the chemical composition of chickpea

A basic procedure was developed to produce a fermented product by solid substrate fermentation using Rhyzopus oligosporus and chickpea as substrate. Water activity was kept at 0.92 throughout the process. Fermentation increased total, ‘true’ and soluble proteins, soluble solids and soluble carbohydrates, and decreased fiber content and pH. About 12% of solids were lost during 72 h of fermentation. The content of most fatty acids was enhanced by fermentation, whereas peroxide value and tannins declined. The color of the fermented product was not deteriorated after 72 h of fermentation. Scanning electron microscopy studies of microbial growth on the substrate showed penetration of the fungus hyphae and degradation effects on the chickpea cotyledon cells.     

玉米灵芝菌粮营养成分及加工特性变化研究

玉米作为主要的杂粮谷物,营养价值高,维生素、膳食纤维等含量丰富,可以预防多种亚健康疾病,受到市场追捧。但是玉米粉营养结构不均衡、加工性差,限制其应用。有研究表明,微生物发酵技术可以改善谷物的营养成分、大分子物质结构和加工特性。基于此,利用灵芝固态发酵玉米,得到玉米灵芝菌粮（简称菌粮）,从营养成分、大分子物质结构和加工特性3个方面对其进行评价。结果显示,与未发酵玉米相比,菌粮中碳水化合物、蛋白质含量分别提高了748%、28.00%,且蛋白质的氨基酸评分提高,而脂肪含量降低了52.56%;维生素C、核黄素和烟酸含量均显著提高（P<0.05）,分别提高了56.19%、73.91%和20.27%,且玉米中缺乏的硫胺素在菌粮中被检测到;菌粮中各类淀粉和纤维的含量也发生了显著变化（P<0.05）,淀粉、支链淀粉含量分别降低了11.17%、34.70%,直链淀粉含量提高了26.66%,粗纤维、不溶性膳食纤维含量分别降低了21.07%、21.47%,可溶性膳食纤维含量提高了13.57%;菌粮粉粘度降低,水溶性指数提高,吸水性指数和溶胀力降低;此外,与灵芝子实体相比,菌粮中灵芝三萜和灵芝酸含量均显著提高（P<0.05）,分别为灵芝子实体的1.68和2.07倍。灵芝固态发酵玉米得到的玉米灵芝菌粮,营养结构更加均衡,功能活性提高,具有更高的营养价值;大分子物质结构发生改变,加工特性得到改善,冲调特性更好。研究结果为食用菌发酵改良谷物特性的研究提供了参考和指导。     

Efficient leaching of cellulases produced byTrichoderma harzianum in solid state fermentation

Summary Recovery of cellulases from solid state cultures ofTrichoderma harzianum was efficiently achieved by hydraulic pressing. Pressing of fermented solids yielded carboxymethyl-cellulase (CMCase) extraction efficiency of 71% and a ratio of leachate to fermented solids of 0.58 (v/w). Addition of water to pressed solids and second pressing improved the efficiency (95%) with simultaneous increase in the ratio to 1.16 (v/w). The overall extraction of filter paper activity was lower (85%) than that of CMCase. This technique is simple and its extraction efficiency is similar to that obtained in multiple-contact counter-current systems. The hydraulic press in its individuality was not used earlier to leach the product from fermented solids.     

Growth of Bifidobacterium longum BB536 in medida (fermented cereal porridge) and their survival during refrigerated storage

AIMS: To develop medida, a Sudanese fermented thin porridge as a probiotic dietary adjunct with high total solids. METHODS AND RESULTS: Fifteen per cent brown rice flour of 2-day-old malted paddy and skim milk were used for formulation. Levels of 2.25, 4.5 and 10% of added skim milk were studied. The initial pH was 6.7 and fermentation was run to a final pH of 4.4 using culture of Bifidobacterium longum BB 536. The highest count of 9.9 +/- 0.07 log CFU ml(-1) was obtained with 10% of added skim milk. The total solids at this level was 21%, 11.1 times more compared with the traditionally prepared medida using un-malted brown rice. The viscosity was low and the flowing characteristic was stable. The final productions of lactic and acetic acids were 56.8 +/- 0.80 and 56.3 +/- 2.00 mumol ml(-1) respectively. The high ratio of acetate to lactate decreased as fermentation continues due to the increase in the rate of lactate production. Under refrigerated storage the count of B. longum BB 536 remained relatively stable during the first week (9.7 +/- 0.10 log CFU ml(-1)) then subsequently decreased by 0.9 log CFU ml(-1) in the following week. CONCLUSIONS: The results of this study demonstrated that fermented medida made from malted brown rice is a suitable food system for the delivery of B. longum BB 536 with a relatively stable shelf life. SIGNIFICANCE AND IMPACT OF THE STUDY: The present study is the first attempt to prepare fermented medida from malted flour with bifidobacteria having the highest total solids while still maintaining the flowing characteristics. Previous studies on medida did not go beyond the use of alpha amylase enzyme and pure lactic acid bacteria isolates from spontaneously fermented dough.     

Effects of fermented rooibos (Aspalathus linearis) on adipocyte differentiation

Rooibos (Aspalathus linearis) contains a rich complement of polyphenols, including flavonoids, considered to be largely responsible for its health promoting effects, including combatting obesity. The purpose of this study was to examine the effect of fermented rooibos hot water soluble solids on in vitro adipocyte differentiation by using differentiating 3T3-L1 adipocytes. Hot water soluble solids were obtained when preparing an infusion of fermented rooibos at “cup-of-tea” strength. The major phenolic compounds (>5 mg/g) were isoorientin, orientin, quercetin-3-O-robinobioside and enolic phenylpyruvic acid-2-O-β-d-glucoside. Treatment of 3T3-L1 adipocytes with 10 μg/ml and 100 μg/ml of the rooibos soluble solids inhibited intracellular lipid accumulation by 22% (p < 0.01) and 15% (p < 0.05), respectively. Inhibition of adipogenesis was accompanied by decreased messenger RNA (mRNA) expression of PPARγ, PPARα, SREBF1 and FASN. Western blot analysis exhibited decreased PPARα, SREBF1 and AMPK protein expression. Impeded glycerol release into the culture medium was observed after rooibos treatment. None of the concentrations of rooibos hot water soluble solids was cytotoxic, in terms of ATP content. Interestingly, the higher concentration of hot water soluble solids increased ATP concentrations which were associated with increased basal glucose uptake. Decreased leptin secretion was observed after rooibos treatment. Our data show that hot water soluble solids from fermented rooibos inhibit adipogenesis and affect adipocyte metabolism, suggesting its potential in preventing obesity.     

Enzymatic pre-hydrolysis and anaerobic degradation of wastewaters with high fat contents

Dairy wastewaters containing elevated fat and grease levels (868 mg l^–1) were treated in an upflow anaerobic sludge blanket reactor (UASB) and resulted in effluents of high turbidity (757 nephelometric turbidity units), volatile suspended solids up to 944 mg l^–1 and COD removal below 50%. When the same dairy wastewater was pre-treated with 0.1% (w/v) of fermented babassu cake containing Penicillium restrictum lipases, turbidity and volatile suspended solids were decreased by 75% and 90%, respectively, and COD removal was as high as 90%.     

Ethanol production from alfalfa fiber fractions by saccharification and fermentation

This work describes ethanol production from alfalfa fiber using separate hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF) with and without liquid hot water (LHW) pretreatment. Candida shehatae FPL-702 produced 5 and 6.4 g/l ethanol with a yield of 0.25 and 0.16 g ethanol/g sugar respectively by SHF and SSF from alfalfa fiber without pretreatment. With LHW pretreatment using SSF, C. shehatae FPL-702 produced 18.0 g/l ethanol, a yield of 0.45 g ethanol/g sugar from cellulosic solids or ‘raffinate’. Using SHF, it produced 9.6 g/l ethanol, a yield of 0.47 g ethanol/g sugar from raffinate. However, the soluble extract fraction containing hemicelluloses was poorly fermented in both SHF and SSF due to the presence of inhibitors. Addition of dilute acid during LHW pretreatment of alfalfa fiber resulted in fractions that were poorly saccharified and fermented. These results show that unpretreated alfalfa fiber produced a lower ethanol yield. Although LHW pretreatment can increase ethanol production from raffinate fiber fractions, it does not increase production from the hemicellulosic and pectin fractions.     

Fermentability of corn syrups with different dextrose equivalents added to various grape juices

It was found that neither the enzymes of the grapes nor those of wine yeast Saccharomyces ellipsoideus strain 223 attacked the higher polysaccharides present in corn syrups. The alcohol yield of the corn syrups approached but did not quite reach theoretical assuming that all of the dextrose equivalent (DE) solids were fermented. Glucose, sucrose, and 95 DE corn syrup fermented at about the same rate and yielded comparable alcohol contents. At equal solids content, the 42 DE syrup fermented slower in most cases and yielded lower alcohol content than higher DE syrups.     

微生物发酵青蒿叶和叶渣的研究

为扩大青蒿原料的应用途径,延伸青蒿产业链,对青蒿叶和叶渣进行发酵研究。拟开发可用于动物保健的青蒿来源的产品。采用微生物发酵青蒿及青蒿叶渣,检测枯草芽孢杆菌、酿酒酵母菌、植物乳杆菌等菌株发酵青蒿叶和叶渣后其粗蛋白、粗脂肪、粗纤维素以及青蒿素、青蒿乙素、双氢青蒿酸、青蒿酸含量变化。青蒿叶发酵产物及功效成分含量与对照组比较,酵母菌发酵后粗蛋白提高43.05%,植物乳杆菌发酵后粗脂肪提高106%,枯草芽孢杆菌发酵后粗纤维降低43.30%,黑曲霉菌发酵后青蒿素和青蒿乙素分别提高133.27%和88.06%,地衣芽孢杆菌发酵后青蒿酸提高21.49%,枯草芽孢杆菌发酵后双氢青蒿酸提高86.01%;青蒿叶渣发酵产物与对照组比较,植物乳杆菌发酵后粗脂肪提高87.73%,酿酒酵母菌发酵后粗蛋白提高85.30%,枯草芽孢杆菌发酵后粗纤维降低55.67%,枯草芽孢杆菌发酵后双氢青蒿酸提高71.91%,地衣芽孢杆菌发酵后青蒿乙素提高94.71%。微生物发酵青蒿叶和叶渣显著提高其功效成分含量,增加了探索青蒿叶和叶渣发酵产物作为动物保健品的可能性。     

Influence of lactose hydrolysis and solids concentration on alcohol production by yeast in acid whey ultrafiltrate

Alcohol yields of 6.5% were obtained with Saccharomyces cerevisiae in lactasehydrolyzed acid whey permeate containing 30–35% total solids. Maximum alcohol yields obtained with Kluyveromyces fragilis were 4.5% in lactase-hydrolyzed acid whey permeate at a solids concentration of 20% and 3.7% in normal permeate at a solids concentration of 10%. Saccharomyces cerevisiae efficiently converted the glucose present in lactase-hydrolyzed whey permeates containing 5–30% total solids (2–13% glucose) to alcohol. However, the galactose, which comprised about half the available carbohydrate in lactase-hydrolyzed whey, was not utilized by S. cerevisiae, so that even though alcohol yields were higher when this organism was used, the process was wasteful in that a substantial proportion of the substrate was not fermented. For the process to become commercially feasible, an efficient means of rapidly converting both the galactose and glucose to alcohol must be found.     

Hypotriacylglycerolemic and Antiobesity Properties of a New Fermented Tea Product Obtained by Tea-Rolling Processing of Third-Crop Green Tea (Camellia sinensis) Leaves and Loquat (Eriobotrya japonica) Leaves

We manufactured a new fermented tea by tea-rolling processing of third-crop green tea (Camellia sinensis) leaves and loquat (Eriobotrya japonica) leaves. The mixed fermented tea extract inhibited pancreatic lipase activity in vitro, and effectively suppressed postprandial hypertriacylglycerolemia in rats. Rats fed a diet containing 1% freeze-dried fermented tea extract for 4 weeks had a significantly lower liver triacylglycerol concentration and white adipose tissue weight than those fed the control diet lacking fermented tea extract. The activity of fatty acid synthase in hepatic cytosol markedly decreased in the fermented tea extract group as compared to the control group. The serum and liver triacylglycerol- and body fat-lowering effects of the mixed fermented tea extract were strong relative to the level of dietary supplementation. These results suggest that the new fermented tea product exhibited hypotriacylglycerolemic and antiobesity properties through suppression of both liver fatty acid synthesis and postprandial hypertriacylglycerolemia by inhibition of pancreatic lipase.     

Esterification and transesterification reactions catalysed by addition of fermented solids to organic reaction media

We report for the first time both the production of the lipase of Burkholderia cepacia in solid-state fermentation and the biocatalysis of esterification and transesterification reactions through the direct addition of the lyophilised fermented solids to organic reaction media. B. cepacia produced a lipolytic activity equivalent to 108 U of pNPP-hydrolysing activity per gram of dry solids after 72 h growth on corn bran with 5% (v/w) commercial corn oil as the inducer. The fermented solid material was lyophilised and added directly to the reaction medium in esterification and transesterification reactions. A factorial design was used to study the effects on esterification of temperature, alcohol-to-acid molar ratio and amount of lipolytic activity added. All three variables affected the ester yield significantly, with the amount of enzyme being most important. A 94% ester yield was obtained at 18 h at 37 °C, with an alcohol-to-acid molar ratio of 5:1 and 60 U of added lipolytic activity. For the transesterification reaction, a factorial design was undertaken with the variables being the alcohol-to-acid molar ratio and the added lipolytic activity. Ester yields of over 95% were obtained after 120 h. Our results suggest that biocatalysis using direct addition of fermented solids to organic reaction medium should be further explored.     

Solid-substrate fermentation of alfalfa for enhanced protein recovery

Solid-substrate fermentations for extraction of protein from pressed alfalfa residues with Aspergillus sp. QM 9994 aspergillus niger QM 877, and Rhizopus nigricans QM 387 were conducted in shake flasks. Upon reimbibing and second pressing, total protein recovery from alfalfa was increased from 47.2% for control samples and up to 64.5% for fermented samples. Analysis of juice from fermented samples indicated the presence of cellulase as well as pectinase activities. Dialysis cultures of cellulase-producing fungi showed that total biomass production and solids consumption were much higher than those of a mutant strain lacking the ability to produce cellulase, indicating significant utilization of cellulosic materials in alfalfa. The biomass yields in the former case ranged from 39–47% based on total solids consumption. Since some of the cellulosic and other carbohydrate constituents in alfalfa may be converted into fungal protein, final alfalfa residues following protein extraction in a commercial process would be less bulky for storage and handing and would be more digestible as a nonruminant animal feed.     

Recovery of pectolytic enzymes produced by solid state culture of Aspergillus niger

Pectinases are enzymes with a wide range of applications in the food and drink industries. In the present work, the extraction of pectinases produced by Aspergillus niger in a solid state fermentation system was investigated. The purpose was to reduce enzyme losses in the fermented solids and at the same time obtain a crude extract as concentrated as possible. Initially the performances of stirred tank and fixed bed extractors were compared. Polygalacturonase activity and viscosity reducing capacity obtained in the stirred tank system were 105% and 15% superior, respectively. Repeated extractions and multiple stage countercurrent extraction were studied, employing stirred tanks. It was possible to observe that three stages were enough for total recovery of the enzymes contained in the solids. The final enzyme extract obtained by counter-current extraction with three stages showed a polygalacturonase activity 81% higher than the one obtained by one-stage extraction.     

Using Goat’s Milk,Barley Flour,Honey, and Probiotic to Manufacture of Functional Dairy Product

Stirred yogurt manufactured using probiotic culture which usually called Rayeb milk in the Middle East region is one of the most important functional fermented milk products. To increase the health and functionality properties to this product, some ingredients like fruits, cereal, and whey protein are used in production. This study was carried out to prepare functional Rayeb milk from goat’s milk, barley flour (15%) and honey (4%) mixtures using ABT culture. Also, vanilla and cocoa powder were used as flavorings. Adding barley flour and honey to goat’s milk increased curd tension and water-holding capacity and decreased coagulation time and susceptibility to syneresis. The values of carbohydrate, total solids, dietary fiber, ash, total protein, water soluble nitrogen, total volatile fatty acids, unsaturated fatty acids, oleic, linoleic, α-linolenic acids, and antioxidant activity were higher in Rayeb milk supplemented with barley flour and honey than control. The viabilities of Lactobacillus acidophilus and Bifidobacterium lactis Bb12 (Chr. Hansen’s Lab A/S) increased in fortified Rayeb milk. The recommended level of 10⁷ cfu g^?1 of bifidobacteria as a probiotic was exceeded for these samples. Addition of vanilla (0.1%) or cocoa powder (0.5%) improved the sensory properties of fortified Rayeb milk.     

Bacterial fermentation of cheese whey for production of a ruminant feed supplement rich in curde protein.

A simple and efficient process for the production of a ruminant feed supplement, rich in crude protein (defined as total N X 6.25), by bacterial fermentation of cheese whey has been developed. The lactose in unpasteurized whey is fermented to lactate acid by Lactobacillus bulgaricus at a temperature of 43 degrees C and pH 5.5. The lactic acid produced is continually neutralized with ammonia to form ammonium lactate. The fermented product is concentrated by evaporation to a solids content of about 70% and adjusted to pH 6.8 with additional ammonia. The concentrated product contains about 55% crude protein. Approximately 6 to 8% of the crude protein is derived from bacterial cells. 17% from whey proteins, and 75 to 77% from ammonium lactate. The efficiency of conversion of lactose to lactic acid usually exceeds 95%. The fermentation time is greatly reduced upon the addition of 0.2% yeast extract or 0.1% corn steep liquor as a source of growth factors. Whey containing lactose at concentrations up to 7% can be fermented efficiently, but at higher concentrations lactose is fermented incompletely. The process has been scaled up to a pilot plant level, and 40 tons of concentrated product were produced fro animal feeding trials, without ever encountering putrefactive spoilage.     

Bacterial fermentation of cheese whey for production of a ruminant feed supplement rich in curde protein.

A simple and efficient process for the production of a ruminant feed supplement, rich in crude protein (defined as total N X 6.25), by bacterial fermentation of cheese whey has been developed. The lactose in unpasteurized whey is fermented to lactate acid by Lactobacillus bulgaricus at a temperature of 43 degrees C and pH 5.5. The lactic acid produced is continually neutralized with ammonia to form ammonium lactate. The fermented product is concentrated by evaporation to a solids content of about 70% and adjusted to pH 6.8 with additional ammonia. The concentrated product contains about 55% crude protein. Approximately 6 to 8% of the crude protein is derived from bacterial cells. 17% from whey proteins, and 75 to 77% from ammonium lactate. The efficiency of conversion of lactose to lactic acid usually exceeds 95%. The fermentation time is greatly reduced upon the addition of 0.2% yeast extract or 0.1% corn steep liquor as a source of growth factors. Whey containing lactose at concentrations up to 7% can be fermented efficiently, but at higher concentrations lactose is fermented incompletely. The process has been scaled up to a pilot plant level, and 40 tons of concentrated product were produced fro animal feeding trials, without ever encountering putrefactive spoilage.     

Enzyme characterization for hydrolysis of AFEX and liquid hot-water pretreated distillers' grains and their conversion to ethanol

Dried distillers' grains with solubles (DDGS), a co-product of corn ethanol production, was investigated as a feedstock for additional ethanol production. DDGS was pretreated with liquid hot-water (LHW) and ammonia fiber explosion (AFEX) processes. Cellulose was readily converted to glucose from both LHW and AFEX treated DDGS using a mixture of commercial cellulase and beta-glucosidase; however, these enzymes were ineffective at saccharifying the xylan present in the pretreated DDGS. Several commercial enzyme preparations were evaluated in combination with cellulase to saccharify pretreated DDGS xylan and it was found that adding commercial grade (e.g. impure) pectinase and feruloyl esterase (FAE) preparations were effective at releasing arabinose and xylose. The response of sugar yields for pretreated AFEX and LHW DDGS (6wt%/solids) were determined for different enzyme loadings of FAE and pectinase and modeled as a response surfaces. Arabinose and xylose yields rose with increasing FAE and pectinase enzyme dosages for both pretreated materials. When hydrolyzed at 20wt%/solids with the same blend of commercial enzymes, the yields were 278 and 261g sugars (i.e. total of arabinose, xylose, and glucose) per kg of DDGS (dry basis, db) for AFEX and LHW pretreated DDGS, respectively. The pretreated DDGS's were also evaluated for fermentation using Saccharomyces cerevisiae at 15wt%/solids. Pretreated DDGS were readily fermented and were converted to ethanol at 89-90% efficiency based upon total glucans; S. cerevisiae does not ferment arabinose or xylose.     

Physicochemical properties of extrusion-modified konjac glucomannan

Konjac glucomannan was extruded and subsequently ground under four conditions denoted: KGM1 (33% solids, 90 °C), KGM2 (24% solids, 90 °C), KGM3 (24% solids, 90 °C, die restriction), and KGM4 (24% solids, 110 °C). SEM and particle size analysis showed that extruded KGM had slightly larger and rougher particles. The water absorption index was decreased to 47.92-128.80, as compared to 153.64 for the control (KGMC). The crystallinity index increased to 2.97 and 3.42 for KGM3 and KGM4 samples, as compared to 1.72 for the control. Zero-shear viscosity of 0.5% solutions decreased to 0.36-3.01 Pa s. All samples were shear-thinning and data were best fitted by the Cross model. Based on capillary viscometry, molecular weights were decreased to 2.7 × 10⁵-9.9 × 10⁵, as compared to 1.2 × 10⁶ for the control. In most cases, properties were most altered by higher temperature and shear, and to a lesser extent by lower solids in the feed.     

Does change in accessibility with conversion depend on both the substrate and pretreatment technology?

The accessibility of cellulase and xylanase enzymes to glucan and xylan, respectively, and its change with conversion were measured for pure Avicel glucan and poplar solids that had been pretreated by ammonia fiber expansion (AFEX), ammonia recycled percolation (ARP), dilute acid, and lime. Avicel and pretreated solids were digested to various degrees by cellulase together with β-glucosidase enzymes and then cleaned of residual protein via a biological method using Protease. Glucan accessibility was determined by purified CBHI (Cel7A) adsorption at 4 °C, and 4 and 24 h hydrolysis yields were determined for solids loading containing equal amounts of glucan (1.0% w/v) and lignin (1.0% w/v), in two separate sets of experiments. Consistent with our previous study and in contrast to some in the literature, little change in glucan accessibility was observed with conversion for Avicel, but glucan and xylan accessibility for real biomass varied with the type of pretreatment. For example, AFEX pretreated solids showed a negligible change in glucan accessibility for conversion up to 90%, although xylan accessibility seemed to decline first and then remained constant. On the other hand, a substantial decline in glucan and xylan accessibility with conversion was observed for lime pretreated poplar solids, as shown by initial hydrolysis rates. Yet, an increase in CBHI adsorption with conversion for lime pretreated poplar solids suggested the opposite trend, possibly due to increased lignin exposure and/or reduced effectiveness of adsorbed enzyme.