Factors affecting emulsion stability and quality of oil recovered from enzyme-assisted aqueous extraction of soybeans

The objectives of the present study were to assess how the stability of the emulsion recovered from aqueous extraction processing of soybeans was affected by characteristics of the starting material and extraction and demulsification conditions. Adding endopeptidase Protex 6L during enzyme-assisted aqueous extraction processing (EAEP) of extruded soybean flakes was vital to obtaining emulsions that were easily demulsified with enzymes. Adding salt (up to 1.5 mM NaCl or MgCl₂) during extraction and storing extruded flakes before extraction at 4 and 30 °C for up to 3 months did not affect the stabilities of emulsions recovered from EAEP of soy flour, flakes and extruded flakes. After demulsification, highest free oil yield was obtained with EAEP of extruded flakes, followed by flour and then flakes. The same protease used for the extraction step was used to demulsify the EAEP cream emulsion from extruded full-fat soy flakes at concentrations ranging from 0.03% to 2.50% w/w, incubation times ranging from 2 to 90 min, and temperatures of 25, 50 or 65 °C. Highest free oil recoveries were achieved at high enzyme concentrations, mild temperatures, and short incubation times. Both the nature of enzyme (i.e., protease and phospholipase), added alone or as a cocktail, concentration of enzymes (0.5% vs. 2.5%) and incubation time (1 vs. 3 h), use during the extraction step, and nature of enzyme added for demulsifying affected free oil yield. The free oil recovered from EAEP of extruded flakes contained less phosphorus compared with conventional hexane-extracted oil. The present study identified conditions rendering the emulsion less stable, which is critical to increasing free oil yield recovered during EAEP of soybeans, an environmentally friendly alternative processing method to hexane extraction.     

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.     

Enzymatic hydrolysis of cod (Gadus morhua) by-products: Optimization of yield and properties of lipid and protein fractions

The main products of hydrolysis of fish by-products are hydrolysed protein and oil. The aim of this work was to study the effect of initial heat inactivation of endogenous enzymes, addition of water prior to hydrolysis, use of different commercial enzymes and combination of enzymes on the yield and purity of the protein and oil fractions after enzymatic hydrolysis of cod by-products. This study was designed to examine how all these factors were effective for destroying protein–lipid complexes in order to obtain pure oil and protein fractions and reduce the insoluble fraction.

Initial heating of raw material changed both raw material properties and inactivated endogenous enzymes thereby influencing the following hydrolysis. High amount of lipids in raw material combined with initial heating caused formation of protein–lipid complexes which was found in all protein containing fractions. The main constituents of the lipids in the complexes were phospholipids and other polar lipids. Insoluble protein–lipid complexes formed lead to increased amount of sludge, reduced FPH yield and high amount of lipids in FPH. The highest amount of separated oil was obtained in the experiments after initial heating without added water. These treatments also reduce amount of emulsion, which is not a desirable product after hydrolysis. Initial heating caused denaturation of protein, which decreased their emulsifying properties.

Results showed that it is not possible to obtain all desirable quality indicators such as: maximum oil and FPH yield, minimum emulsion and sludge yield and the highest protein recovery in FPH with the lowest amount of lipids in FPH fraction by using only one hydrolysis process. Therefore, the aim and requirements for the final products should be prioritised and defined very clearly before the process is designed taking into account the composition of raw material. Hydrolysis of unheated raw material with Alcalase and addition of water was the best compromise taking into account the mentioned quality indicators.     

Suitability of aspenwood biologically delignified with Pheblia tremellosus for fermentation to ethanol or butanediol

Summary Enzymatic conversion of lignocellulosic material to fuels and chemicals depends on a initial pretreatment to render the cellulose more susceptible to enzymatic attack. Biological delignification of aspenwood with the fungus Phlebia tremellosus was compared to steaming as a pretreatment method.The biologically delignified aspenwood (BDA) had a high pentosan content and did not contain inhibitors of enzymatic hydrolysis or subsequent fermentation. In contrast, the steamed aspenwood required a water extraction step to remove the inhibitory material and this step also removed most of the pentosan. The yield of treated material was 90% from biological delignification and 70% from steaming.The cellulose in the BDA was less accessible to the cellulase enzymes than the steamed aspenwood. Combined hydrolysis and fermentation with Saccharomyces cerevisiae gave a lower yield of ethanol from BDA than from the steamed aspenwood, but the yields based on the weight of substrate before pretreatment were comparable. Combined hydrolysis and fermentation with Klebsiella pneumoniae gave higher yields of butanediol from BDA than from steamed aspenwood, because Klebsiella can ferment the xylose which was present in the biologically treated aspenwood. Trichoderma harzianum produced lower levels of cellulase enzymes when grown on BDA than when grown on steamed aspenwood and this was related to the xylan found in the biologically treated material.Abbreviations BDA biologically delignified aspenwood - SEA-WI steam-exploded, water-extracted aspenwood - AI-SEA-WI acid-impregnated, steam-exploded, water-extracted aspenwood - CHF combined hydrolysis and fermentation - FP filter paper     

Enzymatic oil extraction and positional analysis of ω-3 fatty acids in Nile perch and salmon heads

The use of commercial proteases, bromelain and Protex 30L for oil extraction/recovery of polyunsaturated fatty acids (PUFA) from Nile perch and salmon heads was evaluated. Four phases were obtained after hydrolysis, oily phase, emulsion, aqueous phase and sludge. An increase in water content during the hydrolysis resulted in a decrease in oil yield. Maximum oil yield was obtained when hydrolysis was performed with Protex 30L at 55 °C, without pH adjustment or water addition. An oil yield of 11.2% and 15.7% of wet weight was obtained from Nile perch and salmon heads, respectively, compared to 13.8% and 17.6%, respectively obtained using solvent extraction. Fatty acid distribution analysis showed 50% of palmitic acid was in sn-2 position in Nile perch triglycerides (TAG), while only 16% of this fatty acid was in sn-2 position in salmon oil TAG.     

Oil extraction from Scenedesmus obliquus using a continuous microwave system--design, optimization, and quality characterization

A 1.2 kW, 2450 MHz resonant continuous microwave processing system was designed and optimized for oil extraction from green algae (Scenedesmus obliquus). Algae-water suspension (1:1 w/w) was heated to 80 and 95°C, and subjected to extraction for up to 30 min. Maximum oil yield was achieved at 95°C and 30 min. The microwave system extracted 76-77% of total recoverable oil at 20-30 min and 95°C, compared to only 43-47% for water bath control. Extraction time and temperature had significant influence (p<0.0001) on extraction yield. Oil analysis indicated that microwaves extracted oil containing higher percentages of unsaturated and essential fatty acids (indicating higher quality). This study validates for the first time the efficiency of a continuous microwave system for extraction of lipids from algae. Higher oil yields, faster extraction rates and superior oil quality demonstrate this system's feasibility for oil extraction from a variety of feedstock.     

Enzyme catalyzed biotransformations in aqueous two-phase systems with precipitated substrate and/or product

Biotransformations catalyzed by free and immobilized enzymes have been carried out in aqueous suspensions with up to 25% (w/w) precipitated substrate or product. For the kinetically controlled synthesis of N-Acetyl-Tyr-Arg-NH(2) with up to 0.8 M insoluble activated substrate N-Acetyl-TyrOEt catalyzed by alpha-chymotrypsin (EC3.4.21.1) the dipeptide yield was found to be >90%. This and the space-time yields were higher than those observed for one-phase aqueous systems and much higher than in systems where the insoluble substrate had been solubilized by addition of organic solvents. In the equilibrium controlled hydrolysis of 0.4 M D-phenylglycine-amide catalyzed by immobilized penicillin amidase (EC 3.5.1.11) the product precipitates. The enzyme immobilized in the support with the smallest pores could be reused without reduction in the rate due to precipitation in the pores. This decreases the number of immobilized enzyme molecules that can be used as biocatalysts. The latter was observed for supports with larger pores as the solubility decreases with increasing particle size. These results demonstrate that biotransformations with insoluble substrates or products using free or immobilized enzymes can be easily carried out in aqueous two-phase systems, without organic solvents, provided that the pore sizes of the supports are sufficiently small and that the rate of mass transfer from the precipitated substrate is large. The latter increases with decreasing particle size. (c) 1995 John Wiley & Sons, Inc.     

Isolation and Characterization of Antioxidation Enzymes from Cells of Zedoary (Curcuma zedoaria Roscoe) Cultured in a 5-l Bioreactor

In this study, a cell suspension culture system for zedoary (Curcuma zedoaria Roscoe) was developed, using 50 g/l of fresh weight inoculum in a batch culture. The highest cell biomass obtained from a 5-l bioreactor equipped with three impellers after 14 days of culture was utilized to extract secondary metabolites (essential oil and curcumin) and determine the activities of antioxidant enzymes (peroxidase, superoxide dismutase, and catalase). For essential oil and curcumin, zedoary extracts were recovered via a variety of methods: steam distillation, volatile solvents, and Soxhlet. After 14 days of culture using volatile solvents, the optimal yield of essential oil (1.78%) was obtained when using petroleum ether at 40°C in 6 h of extraction, and the best curcumin yield (9.69%) was obtained at 60°C in 6 h via extraction with 90% ethanol. The activities of antioxidant enzymes from zedoary cells were also assessed. The specific activities of peroxidase, superoxide-dismutase, and catalase reached maximum values of 0.63 U/mg of protein, 16.60 U/mg of protein, and 19.59 U/mg of protein after 14 days of culture, respectively.     

Enzymatic hydrolysis and extraction of arachidonic acid rich lipids from Mortierella alpina

A novel method for efficient arachidonic acid rich lipids extraction was investigated. Six different enzymes (papain, pectinase, snailase, neutrase, alcalase and cellulase) were used to extract lipids from Mortierella alpina. The effects of enzyme concentration, temperature and hydrolysis time on oil recovery were evaluated using factorial experimental design and polynomial regression for each enzyme. Hydrolysis time is found to be the most important parameter for all enzymes. The ratios of enzyme mixtures were also studied. It showed that the mixtures of pectinase and papain (5:3, v/v), pectinase and alcalase (5:1, v/v) were better combined effects on oil yields. The effects of hydrolysis time and temperature were then analyzed by response surface methodology, and oil recoveries were satisfactory (104.6% for pectinase and papain and 101.3% for pectinase and alcalase). In the whole process, the lipid composition was not affected by the enzyme treatments according to fatty acid profile.     

Degradation of starchy substrates by a crude enzyme preparation and utilization of the hydrolysates for lactic fermentation

An enzyme preparation obtained from Aspergillus ustus, possessing cellulase, α-amylase, amyloglucosidase, proteinase and d-xylanase activities, was used along with commercial bacterial α-amylase and amyloglucosidase for the degradation of ragi (Eleusine coracana) flour and wheat (Triticum vulgare) bran. Lactic acid yield from ragi hydrolysate, adjusted to 5% reducing sugars (w/v), was 25% when fermented with Lactobacillus plantarum. The yields increased to 78% and 94% when the ragi hydrolysate was fortified with 20% and 60% (v/v) wheat bran hydrolysate, respectively. When commercial α-amylase and amyloglucosidase were used for the hydrolysis of ragi and wheat bran and L. plantarum was employed to ferment the hydrolysates containing 5% reducing sugars (w/v), lactic acid yields were 10% in ragi hydrolysate and 57% and 90% when the ragi hydrolysate was fortified with 20% and 60% (v/v) of wheat bran hydrolysate, respectively. α-Amylase and amyloglucosidase hydrolysed wheat bran added at 20% (v/v) as the sole source of nutrient to soluble starch hydrolysate (5% reducing sugars) gave 22% yield of lactic acid. The yield increased to 55% by the utilization of A. ustus enzyme preparation in addition to α-amylase and amyloglucosidase for wheat bran hydrolysis.     

纳米器件对叶蛋白提取的影响

从植物中提取蛋白质包括机械破碎和离心等一系列步骤,蛋白质在提取液中的溶解度直接影响蛋白提取率和产量.结果表明,用纳米器件处理过的提取液能显著提高叶蛋白的提取率,提升幅度为10％-30％.利用正交试验研究不同提取条件下纳米器件对蛋白可溶性的影响,结果显示浸泡时长(纳米器件浸泡在提取液中的时长)是最关键的已测因素.此外,植物样品的破碎程度也是影响叶蛋白提取率的关键因素之一.     

A novel process for extraction of edible oils: Enzyme assisted three phase partitioning (EATPP)

Three phase partitioning (TPP), a technique used in protein purification has been evaluated, for extraction of oil from three different plant sources viz: mango kernel, soybean and rice bran. The process consists of simultaneous addition of t-butanol (1:1,v/v) and ammonium sulphate (w/v) to a crude preparation/slurry. Under optimized condition, the protein appears as an interfacial precipitate between upper t-butanol containing oil and lower aqueous phase. Pretreatment of the slurries with a commercial enzyme preparation of proteases, Protizyme, followed by three phase partitioning resulted in 98%, 86% and 79% (w/w) oil yields in case of soybean, rice bran and mango kernel, respectively. The efficiency of the present technique is comparable to solvent extraction with an added advantage of being less time consuming and using t-butanol which is a safer solvent as compared to n-hexane used in conventional oil extraction process.     

Immobilization of α-amylase and amyloglucosidase onto ion-exchange resin beads and hydrolysis of natural starch at high concentration

α-Amylase was immobilized on Dowex MAC-3 with 88 % yield and amyloglucosidase on Amberlite IRA-400 ion-exchange resin beads with 54 % yield by adsorption process. Immobilized enzymes were characterized to measure the kinetic parameters and optimal operational parameters. Optimum substrate concentration and temperature were higher for immobilized enzymes. The thermal stability of the enzymes enhanced after the immobilization. Immobilized enzymes were used in the hydrolysis of the natural starch at high concentration (35 % w/v). The time required for liquefaction of starch to 10 dextrose equivalent (DE) and saccharification of liquefied starch to 96 DE increased. Immobilized enzymes showed the potential for use in starch hydrolysis as done in industry.     

One-step enzyme extraction and immobilization for biocatalysis applications

An extraction/immobilization method for HIs(6) -tagged enzymes for use in synthesis applications is presented. By modifying silica oxide beads to be able to accommodate metal ions, the enzyme was tethered to the beads after adsorption of Co(II). The beads were successfully used for direct extraction of C. antarctica lipase B (CalB) from a periplasmic preparation with a minimum of 58% activity yield, creating a quick one-step extraction-immobilization protocol. This method, named HisSi Immobilization, was evaluated with five different enzymes [Candida antarctica lipase B (CalB), Bacillus subtilis lipase A (BslA), Bacillus subtilis esterase (BS2), Pseudomonas fluorescence esterase (PFE), and Solanum tuberosum epoxide hydrolase 1 (StEH1)]. Immobilized CalB was effectively employed in organic solvent (cyclohexane and acetonitrile) in a transacylation reaction and in aqueous buffer for ester hydrolysis. For the remaining enzymes some activity in organic solvent could be shown, whereas the non-immobilized enzymes were found inactive. The protocol presented in this work provides a facile immobilization method by utilization of the common His(6) -tag, offering specific and defined means of binding a protein in a specific location, which is applicable for a wide range of enzymes.     

Xylan extraction from pretreated sugarcane bagasse using alkaline and enzymatic approaches

Background

New biorefinery concepts are necessary to drive industrial use of lignocellulose biomass components. Xylan recovery before enzymatic hydrolysis of the glucan component is a way to add value to the hemicellulose fraction, which can be used in papermaking, pharmaceutical, and food industries. Hemicellulose removal can also facilitate subsequent cellulolytic glucan hydrolysis.

Results

Sugarcane bagasse was pretreated with an alkaline-sulfite chemithermomechanical process to facilitate subsequent extraction of xylan by enzymatic or alkaline procedures. Alkaline extraction methods yielded 53% (w/w) xylan recovery. The enzymatic approach provided a limited yield of 22% (w/w) but produced the xylan with the lowest contamination with lignin and glucan components. All extracted xylans presented arabinosyl side groups and absence of acetylation. 2D-NMR data suggested the presence of O-methyl-glucuronic acid and p-coumarates only in enzymatically extracted xylan. Xylans isolated using the enzymatic approach resulted in products with molecular weights (Mw) lower than 6 kDa. Higher Mw values were detected in the alkali-isolated xylans. Alkaline extraction of xylan provided a glucan-enriched solid readily hydrolysable with low cellulase loads, generating hydrolysates with a high glucose/xylose ratio.

Conclusions

Hemicellulose removal before enzymatic hydrolysis of the cellulosic fraction proved to be an efficient manner to add value to sugarcane bagasse biorefining. Xylans with varied yield, purity, and structure can be obtained according to the extraction method. Enzymatic extraction procedures produce high-purity xylans at low yield, whereas alkaline extraction methods provided higher xylan yields with more lignin and glucan contamination. When xylan extraction is performed with alkaline methods, the residual glucan-enriched solid seems suitable for glucose production employing low cellulase loadings.

     

Oxidation and Structural Modification of Full-Fat and Defatted Flour Based Soy Protein Isolates Induced by Natural and Synthetic Extraction Chemicals

Soy protein has been extracted and differently treated to yield products of diverse desirable characteristics. Generally, synthetic chemicals (NaOH and HCl) are used to extract the protein from n-hexane-defatted soy flour (DF). Some researchers have tried to extract it from full-fat flour (FF) using natural chemicals (NC) in response to the ever-increasing consumer preference for naturally processed foods. The effects of these chemicals on the structure of the resultant protein product are not known. This study examined oxidative and structural modification effects of NC and SC as they interact with proteins in the DF and FF systems. Significant differences (p?<?0.01) were observed in all samples in lipoxygenase activity, degree of oxidation, free and total sufhydryl content and intrinsic fluorescence, which indicated increased structural changes in the FF-based samples as compared to those prepared from DF. Circular dichroism spectroscopy showed existence of α-helices and β-sheets protein secondary structures. However, DF samples showed increase in unordered structural conformation changes than the FF sample. Surface hydrophobicity and size exclusion chromatography results were more related to the extraction chemicals than the type of flour used, with samples prepared with SC showing an increase. That’s, the use of natural and synthetic protein extraction chemicals from FF and DF have different effects on the structure and degree of oxidation of the resultant proteins.     

Particle size distribution of rice flour affecting the starch enzymatic hydrolysis and hydration properties

Rice flour is becoming very attractive as raw material, but there is lack of information about the influence of particle size on its functional properties and starch digestibility. This study evaluates the degree of dependence of the rice flour functional properties, mainly derived from starch behavior, with the particle size distribution. Hydration properties of flours and gels and starch enzymatic hydrolysis of individual fractions were assessed. Particle size heterogeneity on rice flour significantly affected functional properties and starch features, at room temperature and also after gelatinization; and the extent of that effect was grain type dependent. Particle size heterogeneity on rice flour induces different pattern in starch enzymatic hydrolysis, with the long grain having slower hydrolysis as indicated the rate constant (k). No correlation between starch digestibility and hydration properties or the protein content was observed. It seems that in intact granules interactions with other grain components must be taken into account. Overall, particle size fractionation of rice flour might be advisable for selecting specific physico-chemical properties.     

响应面法优化超临界CO2萃取茉莉花蕾精油及抗氧化活性的研究

为研究超临界CO2萃取茉莉花蕾获得精油的最佳工艺及抗氧化活性,实现资源的综合利用。实验考察了夹带剂用量、原料颗粒大小、萃取压力、萃取温度和动态萃取时间对茉莉精油产率的影响,进一步以响应面实验设计优化挥发油的提取工艺参数,以GC-MS分析挥发油组成及相对含量,并测定精油清除DPPH自由基及还原铁离子能力。结果表明,最佳工艺参数为:夹带剂乙醇用量为0.2mL/g,花粉颗粒为40目,萃取压力20MPa,萃取温度46℃,动态萃取时间1.6h。在此条件下茉莉精油的产率为13.67%,远高于同时蒸馏萃取法(2.87%)和超声辅助提取(2.45%)。超临界萃取精油的主要香气成分与茉莉鲜花基本一致,并且具有较好的清除自由基和还原铁离子能力。实验证明超临界萃取技术提取茉莉花蕾得到茉莉精油品质高,可为其资源综合利用提供参考。     

Batch solvent extraction of flavanolignans from milk thistle (Silybum marianum L. Gaertner)

Seeds of milk thistle (Silybum marianum L. Gaertner) contain silymarins and ca. 25% (w/w) of oil. A pre-treatment step involving refluxing with petroleum ether is usually performed before extraction of the silymarins using organic solvents. This paper compares the extraction of whole and defatted milk thistle seeds in various solvents as a function of temperature. The extraction of whole seeds of milk thistle with water at 50, 70 and 85 degrees C was also examined: the yield of silymarin increased with increasing water temperature. In most cases, ethanol at 60 degrees C recovered the largest quantities of silymarins. However, boiling water proved to be an efficient extraction solvent for the more polar silymarins such as taxifolin and silychristin, even when using whole seeds. Extractions of defatted seed meal with boiling ethanol returned maximum yields of 0.62, 3.89, 4.04, and 6.86 mg/g defatted seed of taxifolin, silychristin, silybinin A and silybinin B, respectively. When extracting defatted seed meal with ethanol, yields of taxifolin, silybinin A and silybinin B were, respectively, 6.8-, 0.95-, 1.7- and 1.6-fold higher than when extracting whole seeds. When extracting with boiling water, the yields of silychristin, silybinin A, and silybinin B were 380, 47 and 50% higher for whole seeds compared with defatted seeds.     

In situ alkaline transesterification of cottonseed oil for production of biodiesel and nontoxic cottonseed meal

The production of fatty acid methyl ester (FAME) by direct in situ alkaline-catalyzed transesterification of the triglycerides (TG) in cottonseeds was examined. The experimental results showed that the amount of cottonseed oil dissolved in methanol was approximately 99% of the total oil and the conversion of this oil could achieve 98% under the following conditions: less than 2% moisture content in cottonseed flours, 0.3-0.335mm particle size, 0.1mol/L NaOH concentration in methanol, 135:1 methanol/oil mole ratio, 40 degrees C reaction temperature and 3h reaction time. Further, the effects of co-solvent petroleum ether and methanol recycling on the cottonseed oil extraction and conversion were also investigated. The use of alkaline methanol as extraction and reaction solvent, which would be useful for extraction oil and gossypol, would reduce the gossypol content in the cottonseed meal. The free and total gossypol contents in the cottonseed meal obtained from in situ alkaline transesterification were far below the FAO standard. And the nontoxic cottonseed meal could be used as animal protein feed resources.