Preparation of goat milk powder with Lactobacillus casei L61 and antioxidant peptides: optimization of the composite thermal protectants and evaluation of storage stability

Abstract

The Lactobacillus casei L61 has great ability for producing antioxidant peptides. For reducing the mortality of L. casei L61 in spray drying process, the Box-Behnken design (BBD) was adopted to optimize the composite thermal protective agent formula. The results exhibited that the composite thermal protective agent formula of L. casei L61 contained glucose at 6.03% (w/v), skim milk at 18.98?g/L, and glycerol at 12.50?mL/L. Under the optimal conditions, the average survival of L. casei L61 in the fermented goat milk reached 14.58?±?0.72% after heat treatment at 75?°C for 10?min, which was higher than the control (13.14%). The average hydroxyl free radical scavenging activity of L. casei L61 reached 85.09?±?0.98%, which was not significantly different from the predicted value (86.83%). Therefore, the BBD is feasible for optimizing the composite thermal protective agent formula of L. casei L61. Under the optimal conditions with the inlet air temperature of 130?°C and feed rate of 4.5?mL/min, the maximum viable counts and survival rate of L. casei L61 were 7.46?×?10⁸ cfu/g and 23.41?±?1.28%, respectively. More importantly, the storage stability of antioxidative probiotic goat milk powder was predicted by temperature acceleration test. The shelf life of antioxidative probiotic goat milk powder was estimated to be 352?days at 4?°C and 117?days at 25?°C, embodying the great long-term stability. This study provides a technical reference for industrialized production of probiotic goat milk powder.     

Comparative Study of Approaches based on the Taguchi and ANOVA for Optimising the Leaching of Copper–Cobalt Flotation Tailings

Approaches based on Taguchi and analysis of variance (ANOVA) methods have been proposed for studying the leaching of copper–cobalt flotation tailings. Taguchi method was used to determine the optimum leaching conditions as well the most influential operating parameters. ANOVA was used to determine the relationship between the experimental conditions and yield levels, as well as to define the significances of parameters on the leaching yields. An L₂₅(5⁵) orthogonal array experimental plan was used to assess the effects of initial acidity (25, 50 , 75, 100, and 125?g/L), leaching time (30, 60, 90, 120, and 150?min), temperature (25, 35, 45, 55, and 65°C), pulp density (S/L?=?10, 15, 20, 25, and 30 solid percent), and ferrous iron concentration (0.0, 1.0, 2.5, 5.0, and 7.5?g/L) on individual dissolution of Cu and Co. Under the optimum conditions (50?g/L, 60?min, 45°C, 15%, 2.5?g/L for Cu; and 100?g/L, 60?min, 65°C, 15% and 2.5?g/L for Co), leaching yields were 95.98% Cu and 97.74% Co. pH and Fe²⁺ were found to be key influential parameters of Cu and Co, respectively.     

Application of adaptive neuro-fuzzy interference system on biosorption of malachite green using fir (Abies nordmanniana) cones biomass

Removal of malachite green (MG) onto fir (Abies nordmanniana) cones biomass (FCB) as a lingo-cellulosic-based structure material was investigated in the present study. Characterization of FCB was performed using Fourier transform infra red and scanning electron microscobe analyses. Several parameters (biomass dose and particle size, dye concentration, temperature, and pH) were investigated to determine optimal working conditions. Subsequently, FCB yelded a q_e of 2.2?mg/g for 50?g/L FCB, in an MG solution of 110?mg/L, pH 3.3, at a temperature of 21?°C, on a 0.2-0.4?mm fraction powder after 146?h of contact. Adaptive neuro-fuzzy interference system modeling was applied to experimental data and results showed that predicted model fitted experimental data with R² = 0.994. In a nutshell, it can be concluded that FCB shows good potential for treating MG contaminated waters.     

Structure Elucidation and Evaluation of Antioxidant and Tyrosinase Inhibitory Effect and Mechanism of Proanthocyanidins from Leaf and Fruit of Leucaena Leucocephala

This study aimed to investigate the structural features, antioxidant activity, tyrosinase inhibitory effect, and mechanism of proanthocyanidins from leaf and fruit of Leucaena leucocephala. MALDI-TOF-MS, thiolysis coupled with HPLC-ESI-MS, and ¹³C-NMR confirmed that these proanthocyanidins were complex mixtures of propelargonidins, procyanidins, and prodelphinidins. (Epi)catechin, (epi)gallocatechin, (epi)catechin gallate, and (epi)gallocatechin gallate were the main constitutive units. The findings obtained from enzyme analysis revealed that the proanthocyanidins had inhibitory effects on both monophenolase and diphenolase of tyrosinase. The IC₅₀ values of leaf and fruit proanthocyanidins were 73.5?±?2.7 and 52.3?±?3.5 µg/mL for monophenolase activity, and 27.2?±?1.4 and 16.1?±?1.1 µg/mL for diphenolase activity, respectively. The inhibition of diphenolase by proanthocyanidins were proved to be reversible and mixed type. In addition, it was also found from various antioxidant methods that the proanthocyanidins in leaf and fruit possessed potent DPPH radical scavenging activity with IC₅₀ values of 103.4?±?0.8 and 87.8?±?1.1 µg/mL, ABTS radical scavenging activity with IC₅₀ values of 72.9?±?0.4 and 65.7?±?0.9 µg/mL, and ferric reducing antioxidant power with FRAP values of 3.74?±?0.03 and 4.02?±?0.15?mmol AAE/g, respectively. The results obtained suggested that the proanthocyanidins from leaf and fruit of L. leucocephala might have the potential to be exploited as natural tyrosinase inhibitors and antioxidants.     

Enhanced adenosine triphosphate production by Saccharomyces cerevisiae using an efficient energy regeneration system

The process of ATP biosynthesis from adenosine catalyzed by Saccharomyces cerevisiae was studied using an efficient energy regeneration system. A fractional factorial design (2^9?5) was used to evaluate the effects of different components in the medium. Magnesium chloride, toluene, and acetaldehyde were found to significantly influence ATP production. The concentrations of the three factors were then optimized using central composition design and response surface analysis. Based on the second-order polynomial model obtained from the experiments, the optimal parameters were obtained as follows: adenosine 20 g/L; glucose 67 g/L; S. cerevisiae cells 250 g/L; magnesium chloride 4.37 g/L; potassium dihydrogen phosphate 67 g/L; toluene 1.40 mL/L; acetaldehyde 2.67 mL/L; pH 7.0; and temperature 37.0 °C. Under the condition, the yield and concentration of ATP reached 97.5% and 37 g/L, respectively. The yield was nearly 10% higher than the level before optimization and the concentration increased two-fold. In addition, the utilization efficiency of energy after optimization increased nearly 6%.     

Modeling and optimization of process parameters for supercritical CO2 extraction of Argemone mexicana (L.) seed oil

This research article deals with the determination of optimal conditions of extraction parameters (e.g. temperature (60–100?°C), pressure (200–350?bar), particle size (0.5–1.0?mm), flow rate-CO₂ (5–15?g/min), and the % of co-solvent (0.0–10% of flow rate-CO₂) resulting to the optimal cumulative extraction yield during the supercritical fluid extraction of Argemone mexicana (L.) seed oil with and without a modifier (ethanol) using a supercritical carbon dioxide as solvent. A “five-factors-three-levels” Box-Behnken design under the response surface methodology was used to show independent and interactive effects of extraction parameters. A mathematical regression model was expressed properly by a quadratic second-order polynomial equation. The maximum oil yield (42.86%) from A. mexicana seeds was obtained with the optimal conditions (85?°C, 305?bar, 0.75?mm, 11?g/min, and 9% of flow rate-CO₂) of extraction parameters. The fatty acids analysis of the seed oil was done using gas chromatography and found its suitability as bio-fuel.     

Mathematical model of growth and polyhydroxybutyrate production using microbial fermentation of Bacillus subtilis

Poly-3-hydroxybutyrate (PHB) has been extensively utilized as a biodegradable plastic. The value of substrate inhibition constant (K_I) was also established in shake flask cultures by varying the initial glucose concentration (20–160?g/L) in growth media. Excess carbon source adversely affected the growth of Bacillus subtilis cultures. The production kinetics of PHB was studied using batch fermentation strategy for B. subtilis culture. Batch cultivation was also performed in a 5-L stirred tank bioreactor to obtain a Biomass and PHB yield of 5.25 and 1.6?g/L, respectively. The kinetic data of biomass, PHB production, and substrate consumption was used to estimate the optimized values of the growth and product formation kinetic parameters. Optimal values of kinetic parameters (µ_m value of 0.325, K_S value of 10.53?g/L for glucose, Y value of 0.183?g/g of glucose, K_I value of 105?g/L, m value of 0.12?g/(g h), k₁ of 0.36?g/g, and k₂ value was 0.12?g/(g h)) and the initial values of biomass, substrate and PHB concentration (X?=?0.14?g/L, S?=?9.99?g/L, and P?=?0.13?g/L) were utilized to obtain a modified mathematical model for PHB production. Statistical validity of the mathematical model simulations were measured using F-test. The F-test showed that the statistical validity of the model was more than 95% when compared with experimentally obtained values. This model also predicted that the production of PHB using B. subtilis cultures is mainly growth associated.     

Microwave-assisted extraction as an advanced technique for optimization of saponin yield and antioxidant potential from Phyllanthus amarus

The objective of this study was to apply microwave-assisted extraction (MAE) as an advanced technique for optimization of saponin yield and antioxidant potential from Phyllanthus amarus. The findings indicated that the optimal MAE parameters consisted of 100% methanol, irradiation time 4 s/min, extraction time 50 min, and solvent to sample ratio 50 mL/g. Under these optimal parameters, saponin content (SC), saponin extraction efficiency (SEE), and total phenolic content (TPC) of P. amarus were 229.5 mg escin equivalents (EEs)/g dried sample, 82.8%, and 40.7 mg gallic acid equivalents (GAEs)/g dried sample, respectively. The antioxidant capacity of P. amarus in terms of 2,2ˊ-azino-bis(3-ethylbenzothiazoline-6-sulphonic acid) radical scavenging capacity (ARSC), 2,2-diphenyl-1-picryl-hydrazil radical scavenging capacity (DRSC), and ferric reducing antioxidant power (FRAP) were 487.3, 330.6, and 233.5 mg trolox equivalents (TEs)/g dried sample, respectively. These measured values were not significantly different from the predicted values by response surface methodology (227.9 mg EE/g dried sample, 82.1%, and 39.2 mg GAE/g dried sample for SC, SEE, and TPC and 484.8, 297.3, and 226.6 mg TE/g dried sample for ARSC, DRSC, and FRAP, respectively). Hence, the optimal MAE parameters are suggested for effective extraction of saponins from P. amarus for further investigations and applications.     

AgNPs loaded microemulsion using gallic acid inhibits MCF-7 breast cancer cell line and solid ehrlich carcinoma

Abstract

The objective of this present work is to optimize and prepare silver nanoparticles(AgNPs) in Dioctyl sodium sulfosuccinate (AOT) microemulsion (ME) for oral use and to investigate its antibacterial and anticancer activity in vitro and in vivo. In vitro drug release study confirmed that faster release of drug at the tumor cells compared to the blood circulation. It also showed a potential antibacterial activity against pathogenic bacteria. The optimized AgNPs loaded ME confirmed significant cytotoxicity against MCF-7 cancer cell line with IC50 16.72?±?0.014?μg/mL and significant reduction in solid Ehrlich tumor growth in compared to the control, placebo and pure drug.     

Extraction optimization and adsorption isotherm kinetics of polyphenols from blossoms of Citrus aurantium L. var. amara Engl

ABSTRACT

Crude extracts were extracted from blossoms of Citrus aurantium L. var. amara Engl. with 50% ethanol (CAVAP-E), 50% methanol (CAVAP-M), and hot water (CAVAP-W). CAVAP-W had the highest polyphenol yield of 3.7%. The optimum values of liquid/solid ratio, ultrasonic time, and ultrasonic power were 34.06 mL/g, 1 h, and 81.04 W, respectively. The adsorption characteristics of polyphenols were investigated using different macroporous resins. AB-8 and HP-20 resins offered higher adsorption and desorption capacities. Langmuir equation was more suitable to predict the adsorption of polyphenols. The pseudo second-order model was satisfactory to describe the kinetic data of polyphenols onto AB-8 and HP-20.     

5,8‐Dihydroxy‐9,12,15(Z,Z,Z)‐Octadecatrienoic Acid Production by Recombinant Cells Expressing Aspergillus nidulans Diol Synthase

Whole cells of recombinant Escherichia coli expressing diol synthase from Aspergillus nidulans produced 5,8‐dihydroxy‐9,12,15(Z,Z,Z)‐octadecatrienoic acid from α‐linolenic acid via 8‐hydroperoxy‐9,12,15(Z,Z,Z)‐octadecatrienoic acid as an intermediate. The optimal conditions for 5,8‐dihydroxy‐9,12,15(Z,Z,Z)‐octadecatrienoic acid production using whole recombinant cells were exhibited at pH 7.0, 40 °C, and 250 rpm with 40 g/L cells, 12 g/L, α‐linolenic acid, and 5 % (v/v) dimethyl sulfoxide in a 250‐mL baffled flask containing 50 mL reaction solution. Under these conditions, whole recombinant cells produced 9.1 g/L 5,8‐dihydroxy‐9,12,15(Z,Z,Z)‐octadecatrienoic acid for 100 min, with a conversion yield of 75 % (w/w), a volumetric productivity of 5.5 g/L/h, and specific productivity of 137 mg/g‐cells/h. As an intermediate, 8‐hydroperoxy‐9,12,15(Z,Z,Z)‐octadecatrienoic acid was observed at approximately 1.4 g/L after 100 min. With regard to dihydroxy fatty acid production, this is the highest reported volumetric and specific productivities thus far. This is the first report on the biotechnological production of 5,8‐dihydroxy‐9,12,15(Z,Z,Z)‐octadecatrienoic acid.     

<Emphasis Type="Italic">Penicillium</Emphasis> sp. ZD-Z1 chitosanase immobilized on DEAE cellulose by cross-linking reaction

Chitosanase obtained fromPenicillium sp.ZD-Z1 was immobilized on DEAE cellulose with glutaraldehyde by cross-linking reaction. The optimal conditions of immobilization were as follows: 0.1 g DEAE cellulose was treated with 5 ml 5% glutaraldehyde solution; then 2.3 mg chitosanase was immobilized on the carrier. The optimal temperature and pH was 60 °C and 4.0, and the K _m value was 18.87 g/L. Under optimal conditions, the activity of immobilized enzyme is 1.5 U/g, and the recovery of enzyme activity is 81.3%. After immobilization, the optimal temperature and K _m value increased (from 50 °C to 60 °C, from 2.49 g/L to 18.87 g/L), whereas the optimal pH was reduced (from 5.0 to 4.0). The enzyme activity loss was less than 20% after 10 times batch reaction; the immobilized enzyme showed good operation stability.     

Separation of selected bioactive compounds from orange peel using the sequence of supercritical CO2 extraction and ultrasound solvent extraction: optimization of limonene and hesperidin content

ABSTRACT

The orange peel (Citrus sinensis L.) from the variety Washington Navel was extracted by supercritical CO₂ (SC-CO₂) at different parameters. The extracts were analyzed by gas chromatography-mass spectrometry (GC-MS) and high-performance liquid chromatography (HPLC). Limonene predominance was found (up to 89%). The principal oxygenated monoterpenes were linalool, α-terpineol, decanal, and (E)-citral. Ultrasound-assisted extraction was performed on the remaining solid residue (after SC-CO₂extraction) to obtain the extracts rich in hesperidin. The influence of different extraction parameters on hesperidin content (3.3–23.0 µg/mL) was determined. The prediction performance in optimizing the extraction yield of dominant compounds was studied by response surface methodology and artificial neural network.     

Effect of the condition of spray-drying on the properties of the polypeptide-rich powders from enzyme-assisted aqueous extraction processing

Abstract

Enzyme-assisted aqueous extraction processing (EAEP) is an environmentally friendly technology that simultaneously extracts both oil and protein. It has shown to be commercial feasibility for high oil recovery (～97%) and favorable protein functionality properties. The present study used soy skim, the liquid co-products obtained using EAEP to produce a polypeptide-rich spray-dried powder. The effects of inlet drying air temperature (140?°C, 160?°C, 180?°C and 200?°C), feed flow rate (3, 6, 9, and 12?mL/min), and solids concentration (25%, 30%, 35%, and 40%) on the properties of the polypeptide-rich powders were investigated. Water activity (a_w), color characteristics, bulk density, Carl Index (CI), Water Solubility Index (WSI), micro-morphology, peptide distribution, and antioxidant capacity were significantly affected by different spray-drying parameters. The results of antioxidant capacity test showed that the spray drying conditions significantly affected the antioxidant capacity of the polypeptide-rich powders. The polypeptide molecular weight size and distribution, the composition of the peptide chain, and the cross-linking with other substances could all affect its antioxidant capacity. Overall, good quality polypeptide-rich powders in terms of physicochemical characteristics, micro-morphology, and functional properties can be produced by spray-drying at an inlet temperature of 160?°C, a feed flow rate of 6?mL/min, and solids concentration of 35%.     

Parameter optimization for the enzymatic hydrolysis of sunflower oil in high-pressure reactors

This study is concerned with the hydrolysis of sunflower oil in the presence of lipase preparation Lipolase 100T (Aspergillus niger lipase). Supercritical carbon dioxide was used as a solvent for this reaction. In a high-pressure stirred tank reactor operated in a batch mode, the effects of various process parameters (temperature, pressure, enzyme/substrate ratio, pH, and oil/buffer ratio) were investigated to determine the optimal reaction rate and conversion for the hydrolysis process. The optimal concentration of lipase was 0.0714 g/mL of CO₂-free reaction mixture, and the highest conversions of oleic acid (0.193 g/g of oil phase) and linoleic acid (0.586 g/g of oil phase) were obtained at 50°C, 200 bar, pH=7, and an oil/buffer ratio of 1∶1 (w/w).     

Application of Taguchi method in optimization of desalination by vacuum membrane distillation

This research focuses on desalination via vacuum membrane distillation (VMD). In order to enhance the performance of VMD in desalination and to get more flux, effects of operating parameters on the yield of distillate water were studied. Four parameters at three levels were selected: temperature (35, 45, and 55 °C), vacuum pressure (30, 80, and 130 mbar), flow rate (15, 30, and 60 mL/s) and concentration (50, 100, and 150 g/L). Taguchi method was used to plan a minimum number of experiments. The optimal levels thus determined for the four factors were: temperature 55 °C, vacuum pressure 30 mbar, flow rate 30 mL/s and concentration 50 g/L. The results show that increasing temperature and decreasing vacuum pressure improve permeate flux. However, the permeate flux increases with increasing flow rate initially and then reaches to a maximum value at 30 mL/s and then decreases with increasing the flow rate.     

Biosorption of hexavalent chromium from aqueous solutions using raw coconut fiber as a natural adsorbent

Abstract

This work aims to evaluate the Cr(VI) removal efficiency and adsorption capacity of the raw coconut fiber from synthetic aqueous solutions through the operational parameters as well as to represent the mechanisms of removal by kinetic and isotherm models. The experimental study was conducted in batch system and the optimum conditions for the adsorption of this metal by the biomass were according to: pH 2, contact time of 270?min, and 10?g/L of adsorbent dosage concentration. The removal efficiency obtained for Cr(VI) solutions was 99.2% at concentrations of 25–50?mg/L. For the highest concentrations, the removal decreased from 96.3% to 74.4%, when Cr(VI) solutions ranged from 100?mg/L to 250?mg/L, respectively. The adsorption kinetics was applied and showed a good agreement for pseudo-second-order and Elovich models, which point out a chemisorption. For the adsorption capacity at equilibrium conditions, the best fit was for the Redlich–Peterson isotherm indicating favorable adsorption and monolayer coverage.     

Novel Very Long-Chain α-Methoxylated Δ5,9 Fatty Acids from the Sponge Asteropus niger Are Effective Inhibitors of Topoisomerases IB

The novel fatty acids (2R,5Z,9Z)‐2‐methoxy‐25‐methyl‐5,9‐hexacosadienoic acid ( 1a ) and (2R,5Z,9Z)‐2‐methoxy‐24‐methyl‐5,9‐hexacosadienoic acid ( 1b ) were isolated in 80 % purity from the Caribbean sponge Asteropus niger by chloroform/methanol extraction followed by solvent partitioning and silica gel column chromatography. The compounds were characterized by utilizing a combination of gas chromatography‐mass spectrometry, nuclear magnetic resonance, and circular dichroism. Acids 1a and 1b were not detected in the phospholipids (PtdCho and PtdIns) of the sponge, but rather as free FA and possibly in glycosylceramides. The mixtures of 1a and 1b displayed cytotoxicity towards THP‐1 and HepG2 cells with EC_50's between 41 and 35 μg/mL. Apoptosis was not the preferred mode of cell death induced by 1a – 1b in the THP‐1 cells. This implies other types of cytotoxicity mechanisms, such as membrane disruption and/or the inhibition (EC₅₀ = 1.8 μg/mL) of the human topoisomerase IB enzyme (hTopIB), with a mechanism of inhibition different from the one displayed by camptothecin (CPT). In a separate experiment, the mixture of 1a and 1b also displayed cytotoxicity towards ex vivo mouse splenocytes infected with Leishmania infantum amastigotes (IC₅₀ = 0.17 mg/mL) and free living promastigotes (IC₅₀ = 0.34 mg/mL). It was also found that the FA were inhibitory of the Leishmania topoisomerase IB (LTopIB) with an EC₅₀ = 5.1 μg/mL. Taken together, 1a and 1b represent a new class of FA with potential as TopIB inhibitors that preferentially inhibit hTopIB over LTopIB.     

Pulsed vacuum pickling (PVP) of garlic cloves: Mass transfer kinetics and quality attributes

Abstract

Due to special taste and medicinal properties, pickled sweat-sour garlic is one of the most popular garlic-based functional foods in China. The traditional pickling method of garlic is tedious, time consuming, laborious, low efficient, and easily influenced by environmental factors and microorganisms. In the present study, garlic cloves were subjected to two pickling methods: osmotic dehydration at atmospheric conditions (OD) and pulsed vacuum osmotic dehydration (PVOD). Pulsed vacuum impregnation was applied in order to evaluate the possibility of enhancement of pickling efficiency and quality of final product. The effect of OD and PVOD on mass transfer kinetics of sodium chloride, sucrose and acetic acid as well as quality attributes (color parameters such as L*, a*, b*, and thiosulfinates content) of pickled sweet and sour garlic cloves was investigated. Results indicate that PVOD promoted mass transfer of sodium chloride and acetic acid compared to the traditional OD method. However, there was no significant effect on mass transfer of sugar. PVOD significantly decreased thiosulfinates content (from 4.49?mg/mL to 1.91?mg/mL) and L* values (from 66.72 to 45.85) of garlic. During PVOD of garlic, samples gradually turned from white color to the desired amber color during the PVOD process. The findings of current work indicate that PVOD is a promising technique for garlic pickling as it enhances mass transfer and accelerates the degradation of thiosulfinates content in garlic.     

Improvement of Staphylococcus xylosus lipase production through optimization of the culture conditions

The Staphylococcus xylosus strain produces without induction an original lipase named S. xylosus lipase (SXL). Since considerable interest has been given to microbial lipases for biotechnology applications like detergents, food, drugs and pharmaceutical products, improvement of their production is of great importance to reduce the final cost. This goal could be reached through the optimization of several physicochemical culture conditions. Indeed, an appropriate medium was formulated for SXL production. It was composed of 17 g/L pancreatic digest of casein, 2.5 g/L glucose, 6 g/L yeast extract, 0.75 g/L ammonium sulfate corresponding to a C/N ratio of 6, 1 g/L K₂HPO₄ and 1 g/L KH₂PO₄. In such a medium, SXL production reached 42 U/mL. Moreover, the usefulness of such a medium for large‐scale production of SXL was also evidenced in an automated fully controlled 2.6‐L fermenter. It was shown that aeration of the medium, which strongly affected the growth, regulated the lipase synthesis by the produced cells. It was found that when using a dissolved oxygen saturation of the medium of 50%, the SXL production reached 62 U/mL.