Starch conversion by amylases fromAureobasidium pullulans

Summary A color variant strain (NRRL Y-12974) ofAureobasidium pullulans produced a saccharifying -amylase and two forms of glucoamylase extracellularly when grown on starch at 28°C for 4 days. A sugar syrup containing DP1 (degree of polymerization) and DP2 (31) was made from maltodextrin DE (dextrose equivalent) 10 (35%, w/w) at 55°C and pH 4.5 using the amylase preparation (40 U g^–1 DS (dry substance). The syrup composition was highly dependent upon substrate concentration but nearly independent of enzyme dose. Glucose syrup containing 93% glucose was made from maltodextrin DE 10 (35%, w/w) at 65°C and pH 4.5 using the same enzyme preparation at 100 U g^–1 DS. The enzyme preparation (100 U g^–1 DS) produced 98–100% glucose from raw corn starch at pH 4.5 and 50°C.The mention of firm names or trade products does not imply that they are endorsed or recommended by the US Department of Agriculture over other firms or similar products not mentioned. Abbreviations: DE, dextrose equivalent (an indication of polymerization; reducing sugars as percentage glucose); DP, degree of polymerization; DP1, glucose; DP2, disaccharide; DP3, trisaccharide; DP4, tetrasaccharide; DS, dry substance.     

Monitoring on-line desalted lignocellulosic hydrolysates by microdialysis sampling micro-high performance anion exchange chromatography with integrated pulsed electrochemical detection/mass spectrometry

An on-line system based on microdialysis sampling (MD), micro-high performance anion exchange chromatography (micro-HPAEC), integrated pulsed electrochemical detection (IPED), and electrospray ionization mass spectrometry (MS) for the monitoring of on-line desalted enzymatic hydrolysates is presented. Continuous monitoring of the enzymatic degradation of dissolving pulp from Eucalyptus grandis as well as degradation of sugar cane bagasse in a 5-mL reaction vessel was achieved up to 24 h without any additional sample handling steps. Combining MD with micro-HPAEC-IPED/MS and on-line desalting of hydrolysates enabled injection (5 microL) of at least 23 samples in a study of the sequential action of hydrolytic enzymes in an unmodified environment where the enzymes and substrate were not depleted due to the perm-selectivity of the MD membrane (30 kDa cut-off). Xylanase, phenolic acid esterase and a combination of endoglucanase (EG II) with cellobiohydrolase (CBH I) resulted in the production of DP 1 after the addition of esterase, DP 2 and DP 3 after the addition of EG II and CBH I, from the dissolving pulp substrate. Similar sequential enzyme addition to sugar cane bagasse resulted in DP 1 production after the addition of esterase and DP 1, DP 2 and DP 3 production after the addition of the EG II and CBH I mixture. Combining MS on-line with micro-HPAEC-IPED proved to be a versatile and necessary tool for such a study compared to conventional methods. The mass selectivity of MS revealed complementary information, including the co-elution of saccharides as well as the presence of more than one type of DP 2 in the case of dissolving pulp and several types of DP 2 and DP 3 for sugar cane bagasse. This study demonstrates the limitation of the use of retention time alone for confirmation of the identity of saccharides especially when dealing with complex enzymatic hydrolysates. In situ sampling and sample clean-up combined with on-line desalting of the chromatographic effluent, provides a generic approach to achieve real time monitoring of enzymatic hydrolysates when they are detected by a combination of IPED and MS.     

An alkali-thermotolerant extracellular protease from a newly isolated Streptomyces sp. DP2

Of six alkalitolerant, extracellular protease producing bacterial strains isolated, DP2 displayed maximum activity. This organism was designated as Streptomyces sp. DP2 and identified as Streptomyces ambofaciens. Maximum protease yield was observed after 48 hours of submerged fermentation using various carbon and nitrogen sources. Fructose was found to be the best substrate for protease production, followed by maltose, lactose and wheat bran. Mustard cake is reported for the first time as the most ideal nitrogen source although soybean meal also gave comparable yield. The protease produced by Streptomyces sp. DP2 exhibited extensive activity over a broad pH range (4–12) with maximum activity at pH 8, and was active over a broad range of elevated temperatures (50–100°C), and possessed thermostability at 60–90°C for up to 1 hour. Enzyme activity was reduced by EDTA (25%), SDS (16%), and PMSF (6%). This novel alkaline protease has both alkali- and thermostability that may have industrial significance.     

Production of high-content inulo-oligosaccharides from inulin by a purified endoinulinase

Inulo-oligosaccharides were produced from inulin with high yield by using a purified endoinulinase from a commercial inulinase preparation. The maximum yield of oligosaccharide achieved was around 96% irrespective of substrate concentrations ranged from 50 to 150 g inulin/l. A wide range of degradation products from inulin, varying in their DP (degree of polymerization) 2 to 6, were obtained where the major oligosaccharides were DP3 and 4. The reaction pH gave rise to a significant difference in yield and sugar composition of inulo-oligosaccharides.     

Synthesis of unnatural sugar nucleotides and their evaluation as donor substrates in glycosyltransferase-catalyzed reactions

New unnatural sugar nucleotides, UDP-Fuc and CDP-Fuc were synthesized from fucose-beta-1-phosphate and nucleotide monophosphates activated as morpholidates. Furthermore, a nucleotide analogue was prepared by phosphorylation of 1-(beta-D-ribofuranosyl)cyanuric acid, itself obtained as a protected derivative by condensation of the persilylated derivative of cyanuric acid with 1-O-acetyl-2,3,5-tri-O-benzoyl-beta-D-ribofuranose in 74% yield. This phosphate activated according to the same procedure was condensed with fucose-beta-1-phosphate, affording a new sugar nucleotide conjugate (NDP-Fuc) which was evaluated together with UDP-Fuc, CDP-Fuc and ADP-Fuc, as fucose donors in alpha-(1-->4/3)-fucosyltransferase (FucT-III) catalyzed reaction. Fucose transfer could be observed with each of the donors and kinetic parameters were determined using a fluorescent acceptor substrate. Efficiency of the four analogues towards FucT-III was in the following order: UDP-Fuc=ADP-Fuc>NDP-Fuc>CDP-Fuc. According to the same strategy ADP-GlcNAc was prepared from AMP-morpholidate and N-acetylglucosamine-alpha-1-phosphate; tested as a glucosaminyl donor towards Neisseria meningitidis N-acetylglucosaminyl transferase (LgtA), ADP-GlcNAc was recognized with 0.1% efficiency as compared with UDP-GlcNAc, the natural donor substrate.     

Reaction pattern of a novel thermostable α-amylase

A novel thermostable α-amylase, D45 was studied for its reaction pattern on starch hydrolysis. Fine structures of the dextrins and oligosaccharides produced by D45 were determined and compared with those produced by other thermostable α-amylases, Termamyl^®LC (LC) and Termamyl^®SC (SC). Waxy maize starch dispersion was hydrolyzed with LC, SC and D45 at different concentrations to obtain hydrolysates with the same dextrose equivalent value (DE). At DE 13, molecular weight distribution of dextrins produced by D45 displayed a mono-distribution with a peak centered at degree of polymerization (DP) of 7, whereas LC and SC hydrolysates displayed a bimodal-distribution of the molecular weight profiles with one peak centered at DP 5 and the other at DP 34. Thin-layer chromatograms (TLC) showed that DP 2, 3, 5, 6 and 7 were the primary oligosaccharides produced in LC hydrolysate, DP 4–7 in SC hydrolysate, and DP 6–9 in D45 hydrolysate. Comparison of the decrease in the blue color of amylose-iodine complex at 620 nm (blue value) with the increase in reducing value for the hydrolysis of amylose by LC, SC and D45 showed that for an equivalent decrease in blue value, LC and SC produced a higher percentage of reducing sugar than did D45. The results suggest that D45 has a greater degree of random attack (multichain) reaction, whereas LC and SC have more multiple-attack reactions.     

Production of inulooligosaccharides from inulin by a novel endoinulinase from Xanthomonas sp.

A novel inulinolytic microorganism, Xanthomonas sp. produced an endoinulinase, to be used for inulooligosaccharide (IOS) formation from inulin, at an activity of 11 units ml^–1 (1.2 mg protein ml^–1). The endoinulinase was optimally active at 45°C and pH 6.0. Batchwise production of IOS was carried out by the partially purified endoinulinase with a maximum yield of about 86% on a total sugar basis with 10 g inulin l^–1. The major IOS components were DP (degree of polymerization) 5 and 6 with trace amount of smaller oligosaccharides.     

Development of continuous flow type hydrothermal reactor for hemicellulose fraction recovery from corncob

The semi-pilot scale of continuous flow type hydrothermal reactor has been investigated to separate hemicellulose fraction from corncob. We obtained the effective recovery of hemicellulose using tubular type reactor at 200 °C for 10 min. From constituent sugar analysis of corncob, 82.2% of xylan fraction was recovered as mixture of xylose, xylooligosaccharides and higher-xylooligosaccharide which has more than DP 10. During purification of solubilized fraction by hydrothermal reaction such as ultrafiltration and ion exchange resin, higher-xylooligosaccharide was recovered as the precipitate. This precipitate was identified as non-blanched xylan fraction which has from DP 11 to DP 21 mainly. In this system, only a small amount of furfural has been generated. This tubular reactor has a characteristic controllability of thermal history, and seems to be effective for sugar recovery from soft biomass like corncob.     

Thermo-mechanical extrusion pretreatment for conversion of soybean hulls to fermentable sugars

Thermo-mechanical extrusion pretreatment for lignocellulosic biomass was investigated using soybean hulls as the substrate. The enzyme cocktail used to hydrolyze pretreated soybean hulls to fermentable sugars was optimized using response surface methodology (RSM). Structural changes in substrate and sugar yields from thermo-mechanical processing were compared with two traditional pretreatment methods that utilized dilute acid (1% sulfuric acid) and alkali (1% sodium hydroxide). Extrusion processing parameters (barrel temperature, in-barrel moisture, screw speed) and processing aids (starch, ethylene glycol) were studied with respect to reducing sugar and glucose yields. The conditions resulting in the highest cellulose to glucose conversion (95%) were screw speed 350 rpm, maximum barrel temperature 80 °C and in-barrel moisture content 40% wb. Compared with untreated soybean hulls, glucose yield from enzymatic hydrolysis of soybean hulls increased by 69.6%, 128.7% and 132.2%, respectively, when pretreated with dilute acid, alkali and extrusion.     

Kinetics of batch ethanol fermentation of cheese-whey powder (CWP) solution as function of substrate and yeast concentrations

A lactose utilizing yeast strain, Kluyveromyces marxianus DSMZ-7239 was used for ethanol formation from cheese-whey powder (CWP) solution in batch experiments. Effects of initial substrate (CWP) and yeast concentrations on the rate and extent of ethanol formation were investigated. The initial pH and oxidation-reduction potential (ORP) was kept at 5 and -250 mV, respectively. The rate and extent of ethanol formation increased with increasing CWP concentration up to 156 g l(-1) (75 g l(-1) sugar) and then decreased for larger CWP concentrations due to substrate inhibition at high sugar concentrations. The ethanol yield coefficient was also maximum (0.54 g EtOH/g sugar) and equal to the theoretical yield at CWP concentration of 156 g l(-1). The growth yield coefficient was found to be Y(x/s)=1.2+/-0.1g biomass g sugar(-1). The rate of sugar utilization and ethanol formation also increased linearly with increasing initial biomass concentrations. A kinetic model describing the rate of sugar utilization and substrate inhibition as function of the initial substrate and the biomass concentrations was developed. The kinetic constants were determined using the experimental data. Model predictions of sugar utilization rates were in good agreement with the experimental data. The results indicated that the initial sugar concentration should be below 75 g l(-1) (CWP<156 g l(-1)) and the initial biomass should be above 850 mg l(-1) to obtain high rates and yields of ethanol formation and to avoid substrate inhibition.     

Suitability of commercial beet molasses fractions as substrates fro polyhydroxyalkanoate production byAzotobacter vinelandii UWD

Summary Beet molasses that had been fractionated commercially by ion exclusion resulted in two waste-streams: extract molasses (EM) and concentrated separator by-product (CSB). Only EM at 4–5% w/v contained sufficient sugar to promote polyhydroxybutyrate (PHB) formation byAzotobacter vinelandii UWD, but the yield of PHB/protein was less than that obtained in unfractionated beet molasses. EM and especially CSB added at 0.5–2.0% w/v to media containing a variety of sugar sources promoted an increased yield of PHB/protein. The best use of these beet molasses fractions was, therefore, as a minor addition to media containing sugars to increase PHB yield, but not as a primary substrate for PHB production.     

Acceptor reactions of a novel transfructosylating enzyme from Bacillus sp.

Many different oligosaccharides were produced by transferring the fructose residue of sucrose to maltose, cellobiose, lactose and sucrose (self-transfer), where their yields of fructosylated acceptor products accounted for 26–30% (w/w). The maximum conversion yield (30%) was obtained in fructosyl cellobioside formation with 500 g sucrose l^–1 (substrate) and 200 g cellobiose l^–1 (acceptor). These four acceptors gave various products having DP (degree of polymerization) 2–7 by successive transfer reactions.     

Growth kinetics ofSaccharomyces cerevisiae in batch and fedbatch cultivation using sugarcane molasses and glucose syrup from cassava starch

Growth kinetics ofSaccharomyces cerevisiae in glucose syrup from cassava starch and sugarcane molasses were studied using batch and fed-batch cultivation. The optimum temperature and pH required for growth were 30°C and pH 5.5, respectively. In batch culture the productivity and overall cell yield were 0.31 g L^–1 h^–1 and 0.23 g cells g^–1 sugar, respectively, on glucose syrup and 0.22 g L^–1 h^–1 and 0.18 g cells g^–1 sugar, respectively, on molasses. In fed-batch cultivation, a productivity of 3.12 g L^–1 h^–1 and an overall cell yield of 0.52 g cells g^–1 sugar in glucose syrup cultivation and a productivity of 2.33 g L^–1 h^–1 and an overall cell yield of 0.46 g cells g^–1 sugar were achieved in molasses cultivation by controlling the reducing sugar concentration at its optimum level obtained from the fermentation model. By using an on-line ethanol sensor combined with a porous Teflon^® tubing method in automating the feeding of substrate in the fed-batch culture, a productivity of 2.15 g L^–1 h^–1 with a yield of 0.47 g cells g^–1 sugar was achieved using glucose syrup as substrate when ethanol concentration was kept at a constant level by automatic control.     

Production of inulo-oligosaccharides using endo-inulinase from a pseudomonas sp.

Inulo-oligosaccharides were produced from inulin by using high activities of an endo-acting inulinase. The total yields of oligosaccharide were slightly decreased as the concentration of inulin increased from 50 to 200g/l. Under the optimal reaction conditions, the products consist of inulo-oligosaccharides ranging from DP (degrees of polymerization)2 to DP7, where the major oligosaccharides are 29.8% DP2, 21.4% DP3, and 8.1% DP4 oligomer, respectively. The maximum yield was 75.6% when 50g inulin/l and 15 units/g substrate were used.     

Optimization of enzymatic hydrolysis of mango kernel starch by response surface methodology

Amyloglucosidase (EC 3.2.1.3) from Aspergillus niger was employed for the saccharification of mango (Mangifera indica Linn) kernel starch. Response surface methodology based on a three-level three-factor Box-Behnken design was employed to optimize the important process variables such as substrate concentration (137.5-412.5 mg), enzyme concentration (4-12 mg) and temperature (35-55 °C). The sugar yield increased with both enzyme concentration and temperature, and decreased with substrate concentration. The response surface model indicated optimum conditions (substrate, 137.5 mg; enzyme, 12 mg; temperature, 55 °C) for obtaining 0.4851 mg sugar/mg substrate, which was also verified experimentally.     

Optimizing medium constituents and fermentation conditions for citric acid production from palmyra jaggery using response surface method

The quantitative effects of pH, temperature, time of fermentation, sugar concentration, nitrogen concentration and potassium ferrocyanide on citric acid production were investigated using a statistical experimental design. It was found that palmyra jaggery (sugar syrup from the palmyra palm) is a suitable substrate for increasing the yield of citric acid using Aspergillus niger MTCC 281 by submerged fermentation. Regression equations were used to model the fermentation in order to determine optimum fermentation conditions. Higher yields were obtained after optimizing media components and conditions of fermentation. Maximum citric acid production was obtained at pH 5.35, 29.76 °C, 5.7 days of fermentation with 221.66 g of substrate/l, 0.479 g of ammonium nitrate/l and 2.33 g of potassium ferrocyanide/l.     

Correlation of the properties of several lignocellulosic substrates to the crop performance of the shiitake mushroom Lentinula edodes

Two selected Lentinula edodes strains (S4080 and SIEF0231) were cultivated on oak-wood sawdust (OS), wheat straw (WS) and corn-cobs (CC) substrates in order to examine the influence of those residues on mycelium growth and on basidiomata production. For both strains, mycelial growth measurements conducted in race tubes demonstrated faster colonization of OS and WS media. Lag-phase and complete colonization periods were correlated to mycelium extension rates in the three substrates tested. Similar patterns of pH and electrical conductivity (Ec) changes were detected in all media and for all strains tested; the pH decreased steadily throughout the colonization process to reach values of 4.49–5.06; Ec increased by the end of mycelium colonization, and it presented the highest and lowest values in the WS and OS media respectively. In addition, a negative correlation was established between final salt content of the substrates and mycelium extension rates. Subjecting fully colonized substrates to a cold-shock treatment resulted in fruiting 58–65 days after inoculation in tubes; WS and CC promoted earlier sporophore initiation than OS. Monitoring CO₂ emissions by strain SIEF0231 in pilot-scale cultivation on synthetic blocks, revealed higher respiration rates from OS and CC than from WS, which were further correlated with substrate colonization rates. Among residues colonized by the same strain, WS appeared to promote earliness and crop productivity (BE 54.17%) by presenting shorter cropping periods and equal yield distribution among flushes, while on OS and CC maximum yields were obtained within the first two flushes. Moreover, heavier basidiomata were produced by WS and OS substrates.     

Three‐Enzyme Phosphorylase Cascade for Integrated Production of Short‐Chain Cellodextrins

Cellodextrins are linear β‐1,4‐gluco‐oligosaccharides that are soluble in water up to a degree of polymerization (DP) of ≈6. Soluble cellodextrins have promising applications as nutritional ingredients. A DP‐controlled, bottom‐up synthesis from expedient substrates is desired for their bulk production. Here, a three‐enzyme glycoside phosphorylase cascade is developed for the conversion of sucrose and glucose into short‐chain (soluble) cellodextrins (DP range 3–6). The cascade reaction involves iterative β‐1,4‐glucosylation of glucose from α‐glucose 1‐phosphate (αGlc1‐P) donor that is formed in situ from sucrose and phosphate. With final concentration and yield of the soluble cellodextrins set as targets for biocatalytic synthesis, three major factors of reaction efficiency are identified and partly optimized: the ratio of enzyme activity, the ratio of sucrose and glucose, and the phosphate concentration used. The efficient use of the phosphate/αGlc1‐P shuttle for cellodextrin production is demonstrated and the soluble product at 40 g L^?1 is obtained under near‐complete utilization of the donor substrate offered (88 mol% from 200 mm sucrose). The productivity is 16 g (L h)^?1. Through a simple two‐step route, the soluble cellodextrins are recovered from the reaction mixture in ≥95% purity and ≈92% yield. Overall, this study provides the basis for their integrated production.     

Effect of gamma-ray irradiation on alcohol production from corn

Cracked corn was irradiated with gamma rays at 0-100 Mrad and the effects of the irradiation on sugar yield, susceptibility to enzymatic hydrolysis of starch, yeast growth, and alcohol production were studied. Gamma irradiation at 50 Mrad or greater produced a considerable amount of reducing sugar but little glucose. At lower dosages, gamma irradiation significantly increased the susceptibility of corn starch to enzymatic hydrolysis, but dosages of 50 Mrad or greater decomposed the starch molecules as indicated by the reduction in iodine uptake. About 12.5% reducing sugar was produced by amylase treatment of uncooked, irradiated corn. This amount exceeded the level of sugar produced from cooked (gelatinized) corn by the same enzyme treatment. The yeast numbers in submerged cultivation were lower on a corn substrate that was irradiated at 50 Mrad or greater compared to that on an unirradiated control. About the same level of alcohol was produced on uncooked, irradiated (10(5)-10(6) rad) corn as from cooked (121 degrees C for 30 min) corn. Therefore, the conventional cooking process for gelatinization of starch prior to its saccharification can be eliminated by irradiation. Irradiation also eliminated the necessity of sterilization of the medium and reduced the viscosity of high levels of substrate in the fermentation broth.     

Climate-Induced Changes in Grapevine Yield and Must Sugar Content in Franconia (Germany) between 1805 and 2010

When attempting to estimate the impacts of future climate change it is important to reflect on information gathered during the past. Understanding historical trends may also aid in the assessment of likely future agricultural and horticultural changes. The timing of agricultural activities, such as grape harvest dates, is known to be influenced by climate and weather. However, fewer studies have been carried out on grapevine yield and quality. In this paper an analysis is undertaken of long-term data from the period 1805–2010 on grapevine yield (hl/ha) and must sugar content (°Oe) and their relation to temperature. Monthly mean temperatures were obtained for the same time period. Multiple regression was used to relate the viticulture variables to temperature, and long-term trends were calculated. Overall, the observed trends over time are compatible with results from other long term studies. The findings confirm a relationship between yield, must sugar content and temperature data; increased temperatures were associated with higher yields and higher must sugar content. However, the potential increase in yield is currently limited by legislation, while must sugar content is likely to further increase with rising temperatures.