Vanillin bioproduction from alkaline hydrolyzate of corn cob by Escherichia coli JM109/pBB1

Hydrolysis of corn cob performed for 6 h with 0.5 N NaOH at solid/liquid ratio of 0.084 g/g allowed obtaining a hydrolyzate containing 1171 ± 34 mg/l ferulic acid and 2156 ± 63 mg/l p-coumaric acid that was used as a medium for vanillin bioproduction by the engineered strain Escherichia coli JM109/pBB1. Aiming at maximizing vanillin bioproduction, the effects of medium heat sterilization, one-stage or two-stage pre-cultivation, adaptation of the microorganism to the hydrolyzate and inoculum biomass level were investigated. Biomass pre-cultivated once in unsterilized hydrolyzate was able to effectively convert ferulic and p-coumaric acids to a mixture of vanillin, vanillic acid and vanillyl alcohol provided with the typical vanilla flavor. At initial biomass concentration of 0.5 g_DM/l, maximum values of vanillin concentration (239 ± 15 mg/l), vanillin yield on consumed ferulic acid (0.66 ± 0.03 mol/mol) and vanillin volumetric productivity (10.9 ± 0.7 mg/lh) were obtained after 22 h.     

Kinetics of cellulose hydrolysis by halostable cellulase from a marine Aspergillus niger at different salinities

Kinetics of cellulose hydrolysis with halostable cellulase from a marine Aspergillus niger was analyzed at different salinities. Cellulase activity in 8% NaCl solution was 1.43 folds higher than that in NaCl free solution. Half saturation constant, K_m (15.6260 g/L) and the rate constant of deactivation, K_de (0.3369 g/L h) in 8% NaCl solution was lower than that (18.6364 g/L), 0.3754 (g/L h) in NaCl free solution. The maximum initial hydrolysis velocity, V_max (25.5295 g/L h), in 8% NaCl solution was higher than that in NaCl free solution (25.0153 g/L h). High salinity increased affinity to the cellulase to the substrate and thermostability. Halostable cellulase from a marine Aspergillus niger was valuable for cellulose hydrolysis under high salinity conditions.     

Evaluation of biocomposite-based supports for immobilized-cell xylitol production compared with a free-cell system

This study was conducted to evaluate the importance of aeration in free and immobilized cell systems in an aerated bioreactor for xylitol production from an oat hull hemicellulosic hydrolysate using an integrated process. The aeration rate (AR) or oxygen mass transfer coefficient (k_La) demonstrated a significant role in controlling cell (Candida guilliermondii FTI 20037) regeneration and bioconversion performance in free and immobilized cell systems. In the free cell system, an aeration rate of 1.25 vvm corresponding to k_La of 15.8 1/h resulted in maximum values of product yield (Y_p/s: 0.87 g/g), productivity (Q_p: 0.57 g/l/h), and final xylitol concentration (P_f: 55 g/l) from the hydrolysate with a 74.5 g/l xylose concentration. However, in the aerated immobilized cell system, maximum and almost similar results (almost P_f: 54 g/l, Q_p: 0.57 g/l/h and Y_p/s: 0.84 g/g) were obtained with aeration rates from 1.25 to 1.5 vvm using composites based on polypropylene (PP) and partially delignified fiber (PDF). Composites based on acid treated fiber (ATF) containing a high amount of lignin showed some inhibitory impact on xylose uptake and xylitol formation (P_f: 47 g/l and Q_p < 0.49 g/l/h) with the optimal aeration rate of 1.5 vvm in the initial cycle of the bioconversion; this inhibition impact could be resolved in the next consecutive cycles. The surface modifier polyethyleneimine (PEI) slightly enhanced cell retention in the immobilized form on the ATF-based cell support. This investigation helps fill in the knowledge gaps existing on the integrated processing of the lignocellulosic biomass for xylitol bioproduction and biorefinery industry; however, more scale-up studies are recommended for commercialization.     

Soybean root growth inhibition and lignification induced by p-coumaric acid

The effects of 0.25–2 mM p-coumaric acid, a phenylpropanoid metabolite with recognized allelopathic properties, were tested on root growth, cell viability, phenylalanine ammonia-lyase (PAL) activities, soluble and cell wall-bound peroxidase (POD) activities, hydrogen peroxide (H₂O₂) level and lignin content and its monomeric composition in soybean (Glycine max (L.) Merr.) roots. At ≥0.25 mM, exogenously supplied p-coumaric acid induced premature cessation of root growth, increased POD activity and lignin content and decreased the H₂O₂ content. At ≥0.5 mM, the allelochemical decreased the cell viability and PAL activity. When applied jointly with PIP (an inhibitor of the cinnamate 4-hydroxylase, C4H), 1 mM p-coumaric acid increased lignin content. In contrast, the application of MDCA (an inhibitor of the 4-coumarate:CoA ligase, 4CL) with p-coumaric acid did not increase lignin content. The lignin monomeric composition of p-coumaric acid-exposed roots revealed a significant increase of p-hydroxyphenyl (H) and guaiacyl (G) units. Taken together, these results suggest that p-coumaric acid's mode of action is entry via the phenylpropanoid pathway, resulting in an increase of H and G lignin monomers that solidify the cell wall and restrict soybean root growth.     

Heterologous production of caffeic acid from tyrosine in Escherichia coli

Caffeic acid is a plant secondary metabolite and its biological synthesis has attracted increased attention due to its beneficial effects on human health. In this study, Escherichia coli was engineered for the production of caffeic acid using tyrosine as the initial precursor of the pathway. The pathway design included tyrosine ammonia lyase (TAL) from Rhodotorula glutinis to convert tyrosine to p-coumaric acid and 4-coumarate 3-hydroxylase (C3H) from Saccharothrix espanaensis or cytochrome P450 CYP199A2 from Rhodopseudomonas palustris to convert p-coumaric acid to caffeic acid. The genes were codon-optimized and different combinations of plasmids were used to improve the titer of caffeic acid. TAL was able to efficiently convert 3 mM of tyrosine to p-coumaric acid with the highest production obtained being 2.62 mM (472 mg/L). CYP199A2 exhibited higher catalytic activity towards p-coumaric acid than C3H. The highest caffeic acid production obtained using TAL and CYP199A2 and TAL and C3H was 1.56 mM (280 mg/L) and 1 mM (180 mg/L), respectively. This is the first study that shows caffeic acid production using CYP199A2 and tyrosine as the initial precursor. This study suggests the possibility of further producing more complex plant secondary metabolites like flavonoids and curcuminoids.     

Effect of oxygen supply on biomass and helvolic acid production in submerged fermentation of Cordyceps taii

The entomogenous fungus Cordyceps taii, a traditional Chinese medicinal mushroom, exhibits potent important pharmacological effects and it has great potential for health foods and medicine. In this work, the effects of oxygen supply on production of biomass and bioactive helvolic acid were studied in shake-flask fermentation of C. taii mycelia. The value of initial volumetric oxygen transfer coefficient (K_La) within 10.1–33.8 h⁻¹ affected the cell growth, helvolic acid production and expression levels of biosynthetic genes. The highest cell concentration of 17.2 g/L was obtained at 14.3 h⁻¹ of initial K_La. The highest helvolic acid production was 9.6 mg/L at 10.1 h⁻¹ of initial K_La. The expression levels of three genes encoding hydroxymethylglutaryl-CoA synthase, hydroxymethylglutaryl-CoA reductase and squalene synthase were down-regulated on day 2 and day 8 but up-regulated on day 14 at an initial K_La value of 10.1 h⁻¹ vs. 33.8 h⁻¹, which well corresponded to the helvolic acid biosynthesis in those conditions. The information obtained would be helpful for improving the biomass and helvolic acid production in large-scale fermentation of C. taii.     

Inhibition of cellulases by phenols

Enzyme hydrolysis of pretreated cellulosic materials slows as the concentration of solid biomass material increases, even though the ratio of enzyme to cellulose is kept constant. This form of inhibition is distinct from substrate and product inhibition, and has been noted for lignocellulosic materials including wood, corn stover, switch grass, and corn wet cake at solids concentrations greater than 10 g/L. Identification of enzyme inhibitors and moderation of their effects is of considerable practical importance since favorable ethanol production economics require that at least 200 g/L of cellulosic substrates be used to enable monosaccharide concentrations of 100 g/L, which result in ethanol titers of 50 g/L. Below about 45 g/L ethanol, distillation becomes energy inefficient. This work confirms that the phenols: vanillin, syringaldehyde, trans-cinnamic acid, and hydroxybenzoic acid, inhibit cellulose hydrolysis in wet cake by endo- and exo-cellulases, and cellobiose hydrolysis by β-glucosidase. A ratio of 4 mg of vanillin to 1 mg protein (0.5 FPU) reduces the rate of cellulose hydrolysis by 50%. β-Glucosidases from Trichoderma reesei and Aspergillus niger are less susceptible to inhibition and require about 10× and 100× higher concentrations of phenols for the same levels of inhibition. Phenols introduced with pretreated cellulose must be removed to maximize enzyme activity.     

Characterization,purification, and temperature/pressure stability of polyphenol oxidase extracted from plums (Prunus domestica)

In this study, polyphenol oxidase (PPO) was extracted from Prunus domestica and partially purified by ammonium sulfate precipitation, hydrophobic interaction chromatography, and ion exchange chromatography. The final purification step revealed a 32.81-fold purification, and the molecular mass was estimated to be 65 kDa by SDS-PAGE. The purified PPO showed enzymatic activity mainly toward five substrates, namely catechol, catechin, 4-methyl catechol, chlorogenic acid, and L-3,4-dihydroxyphenylalanine, whereas it showed no activity toward caffeic acid, ferulic acid, p-coumaric acid, p-cresol, and l-tyrosine. The optimum pH and temperature values were 6.0 and 25 °C, respectively. The enzyme showed high stability in the pH range of 5.0–7.0 and in the temperature range of 25–65 °C. The most effective inhibitors of this enzyme were found to be ascorbic acid and l-cysteine. The thermal inactivation followed a first-order kinetic model, with activation energy of E_a 150.46 ± 1.29 kJ/mol. PPO extracted from plum showed stability at high pressure, with enzyme activation at 500 MPa.     

Comparison of batch,fed-batch and continuous well-mixed reactors for enzymatic hydrolysis of orange peel wastes

An alternative potential feedstock for bioethanol in the automotive sector is citrus peel waste (CPW), which can be processed through enzymatic hydrolysis and fermentation. The present work considers mathematical modeling of orange peel wastes (OPW) hydrolysis with the use of free enzymes and compares the performance of batch, fed-batch and continuous well-mixed reactors after introducing appropriate rate equations in dynamic mass balances. MATLAB^® was used for model implementation.Following the Michaelis–Menten approach, the authors used their own kinetic parameters for the pectin hydrolysis rate equation. The parameters were generated in an apposite experimental program for OPW hydrolysis to galacturonic acid with consideration of product inhibition; the corresponding values were obtained after Lineweaver–Burk linearization and are: r_max = 0.28 g/(L min), K_m = 19.80 g/L and K_IGA = 6.96 g/L, respectively. Vice-versa, the authors adopted the Kadam's group kinetic schemes and parameters for cellulose hydrolysis to cellobiose and glucose. The mathematical model of a well-mixed batch reactor was perfectly validated against the experimental results of OPW hydrolysis to galacturonic acid. In the case of a continuous well-mixed reactor, high dilution rates determine low conversion of OPW. The increased complication of fed-batch operation does not add advantages when compared to batch processing.     

Lactic acid and biosurfactants production from hydrolyzed distilled grape marc

Acid hydrolysis of distilled grape marc, an useless agricultural residue from wineries, was carried out using dilute sulfuric acid (1–5%) at several reaction times and 130 °C, in order to obtain monomeric sugars which after supplementation with corn steep liquor (10 g/L) and yeast extract (10 g/L) were used to carry out the fermentation into lactic acid by Lactobacillus pentosus without detoxification stage. Xylose was the main sugar generated followed by glucose and arabinose. Possible inhibitor compounds such as acetic acid liberated from acetyl groups, and furfural and hydroxymethylfurfural generated by sugars dehydration, were produced as degradation byproducts. The hydrolysis stage was optimized by using an incomplete factorial design where the independent variables were the percentage of catalyzer, the reaction time and the temperature. The optima conditions in terms of xylose concentration were 3.3% H₂SO₄, 125 min and 130 °C, but due to the high furfural concentration, two other conditions using lower reaction times (30 and 77.5 min) were also selected to assay the fermentation. Although any condition was feasible to fully utilize the relatively broad spectra of sugars released by the acid hydrolysis, under the shorter reaction time the best results were achieved (Q_P = 0.476 g/L h; Y_P/S = 0.71 g/g) which represents a theoretical yield of 97%. Furthermore, L. pentosus produced 4.8 mg/L of intracellular biosurfactants, measured as biosurfactin, representing a yield of 0.60 mg of intracellular biosurfactant per g of sugars consumed.     

A comparison of a moderately hypofractionated IMRT planning technique used in a randomised UK external beam radiotherapy trial with an in-house technique for localised prostate cancer

AimTo compare the radiotherapy technique used in a randomised trial with VMAT and an in-house technique for prostate cancer.BackgroundTechniques are evolving with volumetric modulated arc therapy (VMAT) commonly used. The CHHiP trial used a 3 PTV forward planned IMRT technique (FP_CH). Our centre has adopted a simpler two PTV technique with locally calculated margins.Materials and methods25 patients treated with FP_CH to 60 Gy in 20 fractions were re-planned with VMAT (VMAT_CH) and a two PTV protocol (VMAT_60/52 and VMAT_60/48). Target coverage, conformity index (CI), homogeneity index (HI), monitor units (MU) and dose to the rectum, bladder, hips and penile bulb were compared.ResultsPTV coverage was high for all techniques. VMAT_CH plans had better CI than FP_CH (p ≤  0.05). VMAT_60/52/48 plans had better CI than VMAT_CH. FP_CH had better HI and fewer MU than VMAT (p ≤  0.05). More favourable rectum doses were found for VMAT _CH than FP_CH (V_48.6, V_52.8, V₅₇, p ≤  0.05) with less difference for bladder (p ≥  0.05). Comparing VMAT_CH to VMAT_60/52/48 showed little differences for the bladder and rectum but VMAT_CH had larger penile bulb doses (V_40.8, V_48.6, mean, D_2, p ≤  0.05). Femoral head doses (V_40.8) were similarly low for all techniques (p = ≥ 0.05).ConclusionVMAT produced more conformal plans with smaller rectum doses compared to FP_CH albeit worse HI and more MU. VMAT_60/52 and VMAT_60/48 plans had similar rectal and bladder doses to VMAT_CH but better CI and penile bulb doses which may reduce toxicity.     

Fatty acid and nutritive quality of chia (Salvia hispanica L.) seeds and plant during growth

The fatty acid (FA) profile, chemical composition, gross energy and organic matter digestibility of chia (Salvia hispanica L.) have been determined in the seed and in the plant collected at five progressive morphological stages from early vegetative to budding stage. The FA analyses disclosed quantitative differences between the plant stages that were characterised by a high percentage of polyunsaturated fatty acids (PUFA), which made up from 752 to 623 g/kg of the total FA of the plant during the growth cycle. The α-linolenic acid (ALA, C_18:3n–3) decreased from 649 g/kg, at the early vegetative stage, to 499 g/kg of the total FA, at the budding stage, while all the other FAs increased with increasing growth stage. The chia seed FAs were also highly unsaturated, with their main components being ALA (641 g/kg of the total FA) and linoleic acid (LA, C_18:2n–6; 188 g/kg of the total FA).The evolution of the quality of chia is closely related to the ageing of the plant. The chia plant provides a forage with a good nutritive value when harvested at a stage before the shooting period. After this, the nutritional quality of the plant considerably decreases with an increase in the fibrous fractions and a dramatical decrease of the crude protein content.     

Stimuli responsive polymorphism of C12NO/DOPE/DNA complexes: Effect of pH,temperature and composition

N,N-dimethyldodecylamine-N-oxide (C₁₂NO) is a surfactant that may exist either in a neutral or cationic protonated form depending on the pH of aqueous solutions. Using small angle X-ray diffraction (SAXD) we observe the rich structural polymorphism of pH responsive complexes prepared due to DNA interaction with C₁₂NO/dioleoylphosphatidylethanolamine (DOPE) vesicles and discuss it in view of utilizing the surfactant for the gene delivery vector of a pH sensitive system. In neutral solutions, the DNA uptake is low, and a lamellar L_α phase formed by C₁₂NO/DOPE is prevailing in the complexes at 0.2 ≤ C₁₂NO/DOPE < 0.6 mol/mol. A maximum of ~ 30% of the total DNA volume in the sample is bound in a condensed lamellar phase L_α^C at C₁₂NO/DOPE = 1 mol/mol and pH 7.2. In acidic conditions, a condensed inverted hexagonal phase H_II^C was observed at C₁₂NO/DOPE = 0.2 mol/mol. Commensurate lattice parameters, a_HC ≈ d_LC, were detected at 0.3 ≤ C₁₂NO/DOPE ≤ 0.4 mol/mol and pH = 4.9–6.4 suggesting that L_α^C and H_II^C phases were epitaxially related. While at the same composition but pH ~ 7, the mixture forms a cubic phase (Pn3m) when the complexes were heated to 80 °C and cooled down to 20 °C. Finally, a large portion of the surfactant (C₁₂NO/DOPE > 0.5) stabilizes the L_α^C phase in C₁₂NO/DOPE/DNA complexes and the distance between DNA strands (d_DNA) is modulated by the pH value. Both the composition and pH affect the DNA binding in the complexes reaching up to ~ 95% of the DNA total amount at acidic conditions.     

Environmental stress and elicitors enhance taxol production by endophytic strains of Paraconiothyrium variabile and Epicoccum nigrum

This study examined the effect of different elicitors (seven, different concentrations) and environmental factors (water activity (a_w), pH) on taxol production by strains of two endophytic fungi, Paraconiothyrium variabile and Epicoccum nigrum, isolated from temperate yew trees. A defined liquid broth medium was modified with elicitors, solute a_w depressors at different pH values. For P. variabile, the best elicitor was salicylic acid at 50 mg/l which gave a taxol yield of 14.7 ± 4.8 μg/l. The study of synergistic effects between elicitor, a_w and pH on taxol production showed that the highest yield of taxol (68.9 ± 11.9 μg/l) was produced under modified ionic stress of 0.98 a_w (KCl) at pH 5 when supplemented with 20 mg/l of salicylic acid. For E. nigrum, serine was the best elicitor which increased yield significantly (29.6 fold) when KCL was used as the a_w depressor (0.98 a_w) at pH 5.0 with 30 mg/l of serine. The maximum taxol yield produced by E. nigrum was 57.1 ± 11.8 μg/l. Surface response models were used to build contour maps to determine the conditions for maximum and marginal conditions for taxol yield in relation to the best elicitor and a_w, and the best pH for the first time. This will be beneficial for identifying key parameters for improvement of taxol yields by endophytic fungi.     

Milk fatty acid composition of dairy cows grazing at two pasture allowances and supplemented with different levels and sources of concentrate

Milk fatty acid (FA) composition of dairy cows from two grazing studies was examined. In the first study, effects of concentrate supplementation and pasture allowance were evaluated using 20 multiparous Holstein cows in five 4 × 4 Latin squares. The four treatments resulted from the combination of two pasture allowances (i.e., low, 25 versus high, 40 kg dry matter/cow/day) and two concentrate supplementation levels (i.e., 0 versus 1 kg concentrate/4 kg milk). No interactions occurred between concentrate supplementation and pasture allowance for milk FA composition. Concentrate supplementation increased short-chain FA content, and reduced the content of long-chain FA, trans11 C18:1, and cis9, trans11 conjugated linoleic acid (CLA) (1.36 versus 1.18 g/100 g). Concentrate supplementation increased saturated FA (58.6 versus 54.0 g/100 g) and reduced unsaturated FA content (39.9 versus 43.8 g/100 g). Grazing at high pasture allowance increased short-, medium-, and long-chain FA content, without affecting cis9, trans11 CLA content. Saturated FA content was higher (57.1 versus 55.6 g/100 g), and unsaturated FA content was lower (41.3 versus 42.5 g/100 g), when cows grazed at high pasture allowance. Concentrate supplementation reduced unsaturated FA and cis9, trans11 CLA in milk of dairy cows grazing at two pasture allowances. In the second study, two experiments evaluated effects of different energy supplements in grazing dairy cows. In Experiment 1, 25 multiparous Holstein cows were assigned to a cracked corn (CC) or a steam flaked corn (SFC) supplement containing 667 g/kg of corn grain plus a pelleted protein/mineral supplement. In Experiment 2, 22 multiparous Holstein cows were assigned to a ground corn grain (GC) or a non-forage fiber (NFF) supplement. The GC supplement contained 850 g/kg of corn grain, and the NFF supplement contained 440 g/kg of non-forage fiber sources (i.e., beet pulp, soyhulls, wheat middlings) that partially replaced corn grain. Milk FA composition was not affected by corn processing or carbohydrate source. The content of short-, medium-, long-chain FA, and cis9, trans11 CLA (2.5 g/100 g in Experiment 1; 2.1 g/100 g in Experiment 2) was similar between supplements in both experiments. The type of supplement did not affect the content of saturated (62.6 g/100 g in Experiment 1; 65.4 g/100 g in Experiment 2) and unsaturated FA (37.5 g/100 g in Experiment 1; 34.6 g/100 g in Experiment 2). Supplementation with supplements differing in the rate and extent of ruminal carbohydrate digestion did not affect the milk FA composition of grazing dairy cows.     

Salt effects on β-glucosidase: pH-profile narrowing

Salts inhibit the activity of sweet almond β-glucosidase. For cations (Cl⁻ salts) the effectiveness follows the series: Cu⁺², Fe⁺² > Zn⁺² > Li⁺ > Ca⁺² > Mg⁺² > Cs⁺ > NH₄⁺ > Rb⁺ > K⁺ > Na⁺ and for anions (Na⁺ salts) the series is: I⁻ > ClO₄⁻ > ⁻SCN > Br⁻ ≈ NO₃⁻ > Cl⁻ ≈ ⁻OAc > F⁻ ≈ SO₄^− 2. The activity of the enzyme, like that of most glycohydrolases, depends on a deprotonated carboxylate (nucleophile) and a protonated carboxylic acid for optimal activity. The resulting pH-profile of k_cat/K_m for the β-glucosidase-catalyzed hydrolysis of p-nitrophenyl glucoside is characterized by a width at half height that is strongly sensitive to the nature and concentration of the salt. Most of the inhibition is due to a shift in the enzymic pK_as and not to an effect on the pH-independent second-order rate constant, (k_cat/K_m)^lim. For example, as the NaCl concentration is increased from 0.01 M to 1.0 M the apparent pK_a1 increases (from 3.7 to 4.9) and the apparent pK_a2 decreases (from 7.2 to 5.9). With p-nitrophenyl glucoside, the value of the pH-independent (k_cat/K_m)^lim (= 9 × 10⁴ M^− 1 s^− 1) is reduced by less than 4% as the NaCl concentration is increased. There is a similar shift in the pK_as when the LiCl concentration is increased to 1.0 M. The results of these salt-induced pK_a shifts rule out a significant contribution of reverse protonation to the catalytic efficiency of the enzyme. At low salt concentration, the fraction of the catalytically active monoprotonated enzyme in the reverse protonated form (i.e., proton on the group with a pK_a of 3.7 and dissociated from the group with a pK_a of 7.2) is very small (≈ 0.03%). At higher salt concentrations, where the two pK_as become closer, the fraction of the monoprotonated enzyme in the reverse protonated form increases over 300-fold. However, there is no increase in the intrinsic reactivity, (k_cat/K_m)^lim, of the monoprotonated species. For other enzymes which may show such salt-induced pK_a shifts, this provides a convenient test for the role of reverse protonation.     

Optimizing l-(+)-lactic acid production by thermophile Lactobacillus plantarum As.1.3 using alternative nitrogen sources with response surface method

The effects of five alternative nitrogen sources, namely, malt sprout (MS), corn steep liquor (CSL), NH₄Cl, NH₄NO₃ and diamine citrate (DC) were investigated on the l-(+)-lactic acid (LA) production by thermophile Lactobacillus plantarum As.1.3. Through the statistical analysis of the results by three steps of response surface methodology (RSM) design, MS and CSL were found to have significant effects on the LA production and their optimal concentrations in the medium should be 16.0 g/L and 12.0 g/L, respectively. The verification of the optimized medium showed that the maximum specific growth rate (μ_m) was 1.09 h⁻¹, the cell yield coefficient (Y_X/S) and the l-(+)-lactic acid yield coefficient (Y_P/S) were 0.233 (OD₆₂₀/g) and 0.98 (g/g), and the maximum volumetric productivity and the average volumetric productivity were 13.0 g/L h and 3.20 g/L h, respectively. The results indicate that the LA production can also be enhanced with the inexpensive nitrogen source alternatives.     

Subcritical water and dilute acid pretreatments for bioethanol production from Melaleuca leucadendron shedding bark

The feasibility of bioethanol production using the lignocellulose of the shedding bark of Melaleuca leucadendron (Paper bark tree) was investigated. The effects of pretreatment parameters (temperature, time and acid concentration) on the yields of sugars and inhibitors, and optimal pretreatment conditions were determined. At very low severity conditions (combined severity factor, CSF ≤ 0.335), 28% of xylan was recovered and this recovery increased with increasing CSF till it peaked to 64.4% (11.2 g xylose L⁻¹) at a CSF of 1.475. However, at CSF > 2.0, xylose yield declined due to degradation. Mild and progressive glucose yield was detected in prehydrolysate at CSF ≥ 1.514, and subsequent enzymatic hydrolysis allowed complete glucan solubilization. Implementing environmentally friendly subcritical water pretreatment at CSF ≤ 0.335 on the shedding bark, about 85% of glucan solubilization was achieved after enzymatic hydrolysis. An industrial Saccharomyces cerevisiae strain readily fermented crude hydrolysate within 12 h, yielding 24.7 g L⁻¹ ethanol at an inoculum size of 2% (v/v), representing a glucose to ethanol conversion rate of 0.475 g g⁻¹ (91% ethanol yield). Based on our findings, the shedding bark is a potential feedstock for bio-ethanol production.     

The study on effective immobilization of lipase on functionalized bentonites and their properties

Three different functionalized bentonites including acid activated bentonite (B_a), organically modified bentonite with cetyltrimethyl ammonium bromide (B_CTMAB) and the composite by acid activation and organo-modification (B_a-CTMAB) were prepared, and used for immobilization of lipase from bovine pancreatic lipase by adsorption. The amount of lipase adsorbed on the functionalized bentonites was in the following sequence: B_a > B_CTMAB > B_a-CTMAB, showing the strongest affinity of B_a for lipase among the three supports. However, the immobilized lipase on B_a-CTMAB showed the highest activity in the hydrolysis of olive oil by 1.67 times of activity of free lipase due to the hydrophobically interfacial activation and enlarged catalytic interface. While, the activity of immobilized lipase on B_a was lower than 20% of free lipase’s activity due to the absence of hydrophobic activation and negative impact of excessive hydrogen ions on the surface. The K_m values for the immobilized lipase on B_a-CTMAB (0.054 g/mL) and B_CTMAB (0.074 g/mL) were both lower than that of free lipase (0.115 g/mL), and the V_max values were higher for the immobilized lipases, exhibiting a higher affinity of the immobilized lipase toward olive oil than free lipase. In comparison to free lipase, the better resistance to heating inactivation, storage stability and reusability of the immobilized lipases on B_a-CTMAB and B_CTMAB were also obtained. The results show that the efficient and stable biocatalysts for industrial application can be prepared by using the low-cost bentonite mineral as the supports.     

Biological control of infective larvae of Ancylostoma spp. in beach sand

BackgroundGeohelminths are parasites that stand out for their prevalence and wide distribution, depending on the soil for their transmission.AimsThe aim of this work was to evaluate the predatory capacity of the fungal isolate of the genus Duddingtonia (CG768) on third stage larvae (L₃) of Ancylostoma spp. in beach sand under laboratory conditions.MethodsIn the assay A five treatment groups and 1 control group were formed. The treatment groups contained 5000, 10,000, 15,000, 20,000 or 25,000 chlamydospores of the fungal isolate and 1000 Ancylostoma spp. L₃ in pots containing 30 g of sand. The control group (without fungus) contained only 1000 Ancylostoma spp. L₃ and distilled water in pots with 30 g of sand.ResultsEvidence of predatory activity was observed at the end of 15 days, where we observed the following percentages of reduction of L₃: Group 1 (4.5%); Group 2 (24.5%); Group 3 (59.2%); Group 4 (58.8%); Group 5 (63%). However, difference was noted (p < 0.01) only at concentrations 15,000, 20,000 and 25,000 in relation to control group. In the assay B two groups were formed in Petri dishes of 9 cm in diameter containing agar water 2% medium. In the treated group, each Petri dish contained 500 Ancylostoma spp. L₃ and 5 g of sand containing the isolate CG 768 at a concentration of 25,000 chlamydospores/g of sand, and the control group (without fungus) contained only 500 L₃. At the end of 7 days the non-predation L₃ of Petri dishes using the method of Baermann were recovered. Difference (p < 0.01) between groups on reducing the average number of Ancylostoma spp. L₃ (percent reduction of 84%) was observed.ConclusionsThe results of this study confirm earlier work on the efficiency of the Duddingtonia genus in the control of Ancylostoma spp. infective larvae.