Optimized enzymatic synthesis of ascorbyl esters from lard using Novozym 435 in co-solvent mixtures

A mild and efficient method for the conversion of fatty acid methyl esters from lard into ascorbyl esters via lipase-catalyzed transesterification in co-solvent mixture is described. A solvent engineering strategy was firstly applied to improve fatty acid ascorbyl esters production. The co-solvent mixture of 30% t-pentanol:70% isooctane (v/v) was optimal. Response surface methodology (RSM) and central composite design (CCD) were employed to estimate the effects of reaction parameters, such as reaction time (12–36 h), temperature (45–65 °C), enzyme amount (10–20%, w/w, of fat acid methyl esters), and substrate molar ratio of fatty acid methyl esters to ascorbic acid (8:1–12:1) for the synthesis of fatty acid ascorbyl esters in co-solvent mixture. Based on the RSM analysis, the optimal reaction conditions were determined as follows: reaction time 34.32 h, temperature 54.6 °C, enzyme amount 12.5%, substrate molar ratio 10.22:1 and the maximum conversion of fatty acid ascorbyl esters was 69.18%. The method proved to be applicable for the synthesis of ascorbyl esters using Novozym 435 in solvent.     

Ability of Vasconcellea × heilbornii lipase to catalyse the synthesis of alkyl esters from vegetable oils

Lipase-catalysed synthesis of alkyl esters is regarded as a potential alternative to chemical catalysis. Owing to its availability as a waste material from the babaco fruit production, its strong lipolytic activity and its natural immobilization, the dried latex of Vasconcellea × heilbornii appears as a good candidate to produce alkyl esters. The ability and performance of this lipase to catalyse the alcoholysis of sunflower oil with various primary alcohols was evaluated in a solvent-free system. A linear correlation between the final reaction rate and the alcohol polarity was established. For methanolysis, the influence of substrates ratio on final conversion rate was studied at different temperatures. At 30 °C, the lipase was inactivated by shaking in a mixture containing more than 0.5 molar equivalents of methanol; the minimum methanol concentration for enzyme deactivation increased with temperature. Moreover, for a 0.5:1 methanol/TAG molar ratio, conversion rates of 73, 66 and 55% were obtained at 30, 40 and 55 °C respectively, showing that the increase of temperature diminished the final methanolysis conversion rate. These facts were associated to the miscibility of methanol in oil and to the thermodynamic state of the medium. To overcome the inactivation of the lipase by methanol, alcoholysis was carried out by fractionated addition of methanol. In those conditions, Vasconcellea × heilbornii latex could catalyse the conversion of 70% of sunflower TAGs in methyl esters at 30 °C.     

Optimized synthesis of (Z)-3-hexen-1-yl caproate using germinated rapeseed lipase in organic solvent

(Z)-3-hexen-1-yl esters are important green top-note components of food flavors and fragrances. Effects of various process conditions on (Z)-3-hexen-1-yl caproate synthesis employing germinated rapeseed lipase acetone powder in organic solvent were investigated. Rapeseed lipase catalyzed ester formation more efficiently with non-polar compared to polar solvents despite high enzyme stability in both types of solvents. Maximum ester yield (90%) was obtained when 0.125 M (Z)-3-hexen-1-ol and caproic acid were reacted at 25 °C for 48 h in the presence of 50 g/L enzyme in heptane. Enzyme showed little sensitivity towards a_w with optimum yield at 0.45, while added water did not affect ester yield. Esterification reduced by increasing molecular sieves (>0.0125%, w/v). The highest yields of caproic acid were obtained with isoamyl alcohol (93%) followed by butanol and (Z)-3-hexen-1-o1 (88%) respectively reflecting the enzyme specificity for straight and branched chain alcohols. Secondary alcohols showed low reactivity, while tertiary alcohol had either very low reactivity or not esterified at all. A good relationship has been found between ester synthesis and the solvent polarity (log P value); while no correlation for the effect of solvents on residual enzyme activity was observed. It may be concluded that germinated rapeseed lipase is a promising biocatalyst for the synthesis of valuable green flavor note compound. The enzyme also showed a wide range of temperature stability (5–50 °C).     

Debaryomyces hansenii fermentation for arabitol production

The fermentation process for arabitol production from glycerol was developed using a Debaryomyces hansenii strain recently selected from a broad screening. The high-producing strain produced arabitol as the only detectable polyol from glycerol. In this work, the pH, dissolved oxygen concentration (DO), inoculum size and magnesium concentration, and the nitrogen-to-phosphorus (N/P) ratio were systematically evaluated for effects on cell growth rate and arabitol productivity. Among those evaluated, the medium with N/P = 9, DO of 5% air saturation and pH 3.5 supported the highest arabitol production. Under these optimal conditions, arabitol production of 40 g/L was achieved in 5 days compared to earlier studies with 15 g/L arabitol in 5 days. Volumetric productivity and specific productivity were successfully improved from 0.13 to 0.33 g/L-h and 0.007 to 0.02 g/g-h respectively with arabitol yield of 55% from glycerol.     

Optimized synthesis of lipase-catalyzed l-ascorbyl laurate by Novozym® 435

l-Ascorbyl laurate is a fatty acid derivative of l-ascorbic acid which can be widely used as a natural antioxidant in both lipid containing food and cosmetic applications. To avoid any possible harmful effects from chemically synthesized product, the enzymatic synthesis appears to be the best way to satisfy the consumer demand for natural antioxidants. The ability of immobilized lipase from Candida antarctica (Novozym^® 435) to catalyze the direct esterification between l-ascorbic acid and lauric acid was investigated. Response surface methodology (RSM) and 5-level-4-factor central composite rotatable design (CCRD) were employed to evaluate the effects of synthesis parameters, such as reaction time (2–10 h), temperature (25–65 °C), enzyme amount (10–50% w/w of l-ascorbic acid), and substrate molar ratio of l-ascorbic acid to lauric acid (1:1–1:5) on percentage molar conversion to l-ascorbyl laurate. Based on the analysis result of ridge max, the optimal enzymatic synthesis conditions were predicted as follows: reaction time 6.7 h, temperature 30.6 °C, enzyme amount 34.5%, substrate molar ratio 1:4.3; and the optimal actual yield was 93.2%.     

Influence of reaction conditions on the selectivity of the synthesis of lactulose with microbial β-galactosidases

Commercial β-galactosidase preparations from Bacillus circulans, Kluyveromyces lactis and Aspergillus oryzae were evaluated as catalysts for the synthesis of lactulose. Among them, the enzyme from A. oryzae was selected for further studies. The effect of reaction conditions was then studied on product composition during the kinetically controlled synthesis of lactulose by transgalactosylation with A. oryzae β-galactosidase. Product composition was not affected by pH, temperature, total initial concentration of sugar (lactose plus fructose) and enzyme to substrate ratio within the ranges studied. However, lactose to fructose ratio strongly influenced product composition being then possible to control the lactulose to galacto-oligosaccharide ratio within ample margins. Maximum lactulose yield (0.282 g of lactulose per g initial lactose) was obtained using 1/8 lactose to fructose molar ratio, 50% (w/w) total initial sugars, 40 °C, pH 4.5 and enzyme to initial lactose ratio equivalent to 200 IU/g.     

Lipase-catalyzed synthesis of palmitanilide: Kinetic model and antimicrobial activity study

Enzymatic syntheses of fatty acid anilides are important owing to their wide range of industrial applications in detergents, shampoo, cosmetics, and surfactant formulations. The amidation reaction of Mucor miehei lipase Lipozyme IM20 was investigated for direct amidation of triacylglycerol in organic solvents. The process parameters (reaction temperature, substrate molar ratio, enzyme amount) were optimized to achieve the highest yield of anilide. The maximum yield of palmitanilide (88.9%) was achieved after 24 h of reaction at 40 °C at an enzyme concentration of 1.4% (70 mg). Kinetics of lipase-catalyzed amidation of aniline with tripalmitin has been investigated. The reaction rate could be described in terms of the Michaelis–Menten equation with a Ping–Pong Bi–Bi mechanism and competitive inhibition by both the substrates. The kinetic constants were estimated by using non-linear regression method using enzyme kinetic modules. The enzyme operational stability study showed that Lipozyme IM20 retained 38.1% of the initial activity for the synthesis of palmitanilide (even after repeated use for 48 h). Palmitanilide, a fatty acid amide, exhibited potent antimicrobial activity toward Bacillus cereus.     

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

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

Removal of acetic acid and sulfuric acid from biomass hydrolyzate using a lime addition–capacitive deionization (CDI) hybrid process

In this study, we developed a lime addition–capacitive deionization (CDI) hybrid process that can efficiently remove acetic acid and sulfuric acid from the model mixture of glucose, xylose, acetic acid, and sulfuric acid, which are the major components from the biomass hydrolyzate by acid hydrolysis. The key parameters of lime addition process (type of lime, amount of lime, stirrer speed, and reaction time) and CDI process (voltage, flow rate, and feed concentration) were also optimized. In the lime addition process, the optimal lime type, (sulfuric acid + acetic acid)/lime molar ratio, stirrer speed, and reaction time for the removal of sulfuric acid were CaCO₃, 1:1, 200 rpm, and 6 min, respectively. For the CDI process, the optimal voltage and flow rate were 1.2 V and 20 mL/min, respectively. The efficiency of acid removal increased as the initial acetic acid concentration decreased. This hybrid process was able to remove 98.08% of sulfuric acid and 76.97% of acetic acid from the mixture of glucose, xylose, acetic acid, and sulfuric acid. The process was able to recover almost all sugar (>99%) at high purity (97.53%).     

A novel transglycosylating β-galactosidase from Enterobacter cloacae B5

A strain of Enterobacter cloacae B5 producing β-galactosidase with transglycosylation activity was isolated from the soil. Its freeze-thawed cells synthesized galacto-oligosaccharides with a high yield of 55% from 275 g/L lactose at 50 °C for 12 h. A novel β-galactosidase capable of glycosyl transfer was purified from this strain. It was a homotetramer with molecular mass of about 442 kDa. The optimal pH and temperature for hydrolysis activity on o-nitrophenyl-β-d-galactopyranoside (oNPGal) were 6.5–10.5 and 35 °C, respectively. The enzyme showed a wide range of acceptor specificity for transglycosylation and catalyzed glycosyl transfer from oNPGal to various chemicals such as galactose, glucose, fructose, arabinose, mannose, sorbose, rhamnose, xylose, cellobiose, sucrose, trehalose, melibiose, inositol, mannitol, sorbitol and salicin, resulting in novel saccharide yields ranging from 0.8% to 23.5%. A gene encoding the enzyme was cloned and the recombinant enzyme from Escherichia coli had similar transglycosylation activity to the natural enzyme.     

A novel mono- and diacylglycerol lipase highly expressed in Pichia pastoris and its application for food emulsifier preparation

A mono- and diacylglycerol lipase (MDL) was cloned from Penicillium cyclopium and expressed in Pichia pastoris strain GS115. The recombinant enzyme was named Lipase GH1. High cell density fermentation was performed by culture in a 7.5-L fermenter using BSMG medium, in which the phosphate in basal salt medium was replaced by sodium glycerophosphate (Na₂GP). The maximal lipase activity detected was 18,000 U per mL, and total protein content in the fermentation supernatant was 3.94 g per L. The activity of the liquid enzyme remained stable under alkaline conditions at 4 °C for 6 months and was 50% after one year. Lipase GH1 was used for the synthesis of mono- and diacylglycerols (MAGs and DAGs), which are commonly used emulsifiers for industrial applications. A conversion rate of 84% after 24 h of reaction was obtained using glycerol/oleic acid molar ratio 11:1, water content 1.5 wt%, enzyme dosage 80 U per g, and reaction temperature 35 °C. Lipase GH1 was more efficient for the synthesis of MAGs and DAGs than was Lipase G50 (a similar, commercially available lipase derived from Penicillium camemberti) when oleic acid was used as an acyl donor. Lipase GH1 has potential for food emulsifier preparation.     

insilico Characterization and Homology Modeling of Arabitol Dehydrogenase (ArDH) from Candida albican

Background: Arabitol dehydrogenase (ArDH) is involved in the production of different sugar alcohols like arabitol, sorbitol, mannitol, erythritol and xylitol by using five carbon sugars as substrate. Arabinose, d-ribose, d-ribulose, xylose and d-xylulose are known substrate of this enzyme. ArDH is mainly produced by osmophilic fungi for the conversion of ribulose to arabitol under stress conditions. Recently this enzyme has been used by various industries for the production of pharmaceutically important sugar alcohols form cheap source than glucose. But the information at structure level as well as its binding energy analysis with different substrates was missing. Results: The present study was focused on sequence analysis, insilico characterization and substrate binding analysis of ArDH from a fungus specie candida albican. Sequence analysis and physicochemical properties showed that this protein is highly stable, negatively charged and having more hydrophilic regions, these properties made this enzyme to bind with number of five carbon sugars as substrate. The predicted 3D model will helpful for further structure based studies. Docking analysis provided free energies of binding of each substrate from a best pose as arabinose -9.8224calK/mol, dribose -11.3701Kcal/mol, d-ribulose -8.9230Kcal/mol, xylose -9.7007Kcal/mol and d-xylulose 9.7802Kcal/mol. Conclusion: Our study provided insight information of structure and interactions of ArDH with its substrate. These results obtained from this study clearly indicate that d-ribose is best substrate for ArDH for the production of sugar alcohols. This information will be helpful for better usage of this enzyme for hyper-production of sugar alcohols by different industries.     

Optimization of Candida sp. 99-125 lipase catalyzed esterification for synthesis of monoglyceride and diglyceride in solvent-free system

Esterification of glycerol and oleic acid catalyzed by lipase Candida sp. 99-125 was carried out to synthesize monoglyceride (MAG) and diglyceride (DAG) in solvent-free system. Beta-cyclodextrin as an assistant was mixed with the lipase powder. Six reaction variables, initial water content (0–14 wt% of the substrate mass), the glycerol/oleic acid molar ratio (1:1–6:1), catalyst load (3–15 wt% of the substrate mass), reaction temperature (30–60 °C), agitator speed (130–250 r/min) and beta-cyclodextrin/lipase mass ratio (0–2) were optimized. The optimal conditions to the synthesis of MAG and DAG were different: the optimal glycerol/oleic acid molar ratio, beta-cyclodextrin/lipase mass ratio, catalyst load and reaction temperature were 6:1, 0, 5%, 50 °C for MAG, and 5:1, 1.5, 10%, 40 °C for DAG, respectively. The optimal water content and agitator speed for both MAG and DAG were 10% and 190 r/min, respectively. Under the optimal conditions, 49.6% MAG and 54.3% DAG were obtained after 8 h and 4 h, respectively, and the maximum of 81.4% MAG plus DAG (28.1% MAG and 53.3% DAG) was obtained after 2 h under the DAG optimal condition. Above 90% purity of MAG and DAG can be obtained by silica column separation.     

Valorization of olive stones for xylitol and ethanol production from dilute acid pretreatment via enzymatic hydrolysis and fermentation by Pachysolen tannophilus

Olive stones are an agro-industrial by-product abundant in the Mediterranean area that is regarded as a potential lignocellulosic feedstock for sugar production. Statistical modeling of dilute-sulphuric acid hydrolysis of olive stones has been performed using a response surface methodology, with treatment temperature and process time as factors, to optimize the hydrolysis conditions aiming to attain maximum d-xylose extraction from hemicelluloses. Thus, solid yield and composition of solid and liquid phases were assessed by empirical modeling. The highest yield of d-xylose was found at a temperature of 195 °C for 5 min. Under these conditions, 89.7% of the total d-xylose was recovered from raw material. The resulting solids from optimal conditions were assayed as substrate for enzymatic hydrolysis, while fermentability of hemicellulosic hydrolysates was tested using the d-xylose-fermenting yeast Pachysolen tannophilus. Both bioprocesses were considerably influenced by enzyme loading and inoculum size. In the enzymatic hydrolysis step, about 56% of cellulose was converted into d-glucose by using an enzyme/solid ratio of 40 FPU g⁻¹, while in the fermentation carried out with a cell concentration of 2 g L⁻¹ a yield of 0.44 g xylitol/g d-xylose and a global volumetric productivity of 0.11 g L⁻¹ h⁻¹ were achieved.     

Biosynthesis of ethyl caproate and other short ethyl esters catalyzed by cutinase in organic solvent

The main objective of this work was to study the enzymatic synthesis of short chain ethyl esters, a group of relevant aroma molecules, by Fusarium solani pisi cutinase in an organic solvent media (iso-octane), and to assess the influence of different parameters on the reaction yield.Cutinase displayed high initial esterification rates in iso-octane, which amounted to 1.15 μmol min⁻¹ mg⁻¹ for ethyl butyrate (C₄ acid chain) and 1.06 μmol min⁻¹ mg⁻¹ for ethyl valerate (C₅ acid chain). High product yields, 84% for ethyl butyrate and 96% for ethyl valerate, were observed after 6 h of reaction, for an initial equimolar concentration of substrates (0.1 M).The highest product yield (97%) was observed for ethyl caproate (C₆) synthesis, a compound which is a part of natural apple and pineapple flavour, for an alcohol:acid molar ratio of 2 (0.2 M ethanol concentration).Cutinase affinity for short chain length carboxylic acids (C₄–C₆) in ester synthesis in iso-octane confirmed previous observations in reversed micellar system.     

Metabolism of sugars to polyols in the boll weevil

When fed to starved adults of Anthonomus grandis, several pentoses and hexoses were metabolized to the corresponding polyols (sugar alcohols). Xylitol, galactitol, arabitol, ribitol, rhamnitol, mannitol, and sorbitol were metabolites of d-xylose, d-galactose and lactose, d-arabinose, d-ribose, l-rhamnose, d-mannose, and d-glucose and d-fructose, respectively. l-Sorbose was not metabolized to a polyol. Large quantities of xylitol and galactitol and intermediate amounts of arabitol, ribitol, and rhamnitol accumulated while only small amounts or traces of mannitol and sorbitol were detected. The limited accumulation of sorbitol in the glucose- and fructose-fed weevils probably was caused by the rapid metabolism of sorbitol to glucose, fructose, trehalose, and glycogen. Each of the ingested sugars, the corresponding polyols, and trehalose were present in the weevil haemolymph. Most of the polyols had never before been detected as metabolites in an insect.     

Optimization and kinetic study on the synthesis of palm oil ester using Lipozyme TL IM

Enzymatic synthesis of palm oil esters (POE) was carried out via alcoholysis of palm oil (PO) and oleyl alcohol (OA) catalyzed by Lipozyme TL IM. The optimum reaction conditions were: temperature: 60 °C; enzyme load: 24.7 wt%; substrate ratio: 1:3 (PO/OA), impeller speed: 275 rpm and reaction time: 3 h. At the optimum condition, the conversion of POE was 79.54%. Reusability study showed that Lipozyme TL IM could be used for 5 cycles with conversion above 50%. The alcoholysis reaction kinetic follows the Ping-Pong Bi-Bi mechanism characterized by the V_max, K_m(PO), and K_m(OA) values of 32.7 mmol/min, 0.3147 mmol/ml and 0.9483 mmol/ml, respectively. The relationship between initial reaction rate and temperature was also established based on the Arrhenius law.     

Purification and functional characterization of the first stilbene glucoside-specific β-glucosidase isolated from Lactobacillus kimchi

This study aimed to develop viable enzymes for bioconversion of resveratrol-glucoside into resveratrol. Out of 13 bacterial strains tested, Lactobacillus kimchi JB301 could completely convert polydatin into resveratrol. The purified enzyme had an optimum temperature of 30–40 °C and optimum pH of pH 5.0 against polydatin. This enzyme showed high substrate specificities towards different substrates in the following order: isorhaponticin >> polydatin >> mulberroside A > oxyresveratrol-3-O-glucoside. Additionally, it rarely hydrolyzed astringin and desoxyrhaponticin. Based on these catalytic specificities, we suggest this enzyme be named stilbene glucoside-specific β-glucosidase. Furthermore, polydatin extracts from Polygonum cuspidatum were successfully converted to resveratrol with a high yield (of over 99%). Stilbene glucoside-specific β-glucosidase is the first enzyme isolated from lactic acid bacteria capable of bio-converting various stilbene glucosides into stilbene.     

Xylitol production from non-detoxified corncob hemicellulose acid hydrolysate by Candida tropicalis

The interest on use of lignocellulose for producing chemicals is increasing as these feedstocks are low cost, renewable and widespread sources of sugars. Corncob is an attractive raw material for xylitol production due to its high content of xylan. In this study, hemicellulose hydrolysate from corncobs without detoxification was used for xylitol production by Candida tropicalis CCTCC M2012462. Compared with prepared xylose medium, xylitol production with dilute acid hydrolysate medium does not seem to influence specific xylose reductase activity. The decrease in xylitol productivity with dilute acid hydrolysate medium is a result of a lower biomass concentration and lag-phase time. It appears that biomass growth rate is essential for xylitol production. In xylitol fermentation with a low initial inhibitors concentration and substrate feeding strategy, a maximal xylitol concentration of 38.8 g l⁻¹ was obtained after 84 h of fermentation, giving a yield of 0.7 g g⁻¹ xylose and a productivity of 0.46 g l⁻¹ h⁻¹.     

Novel minor lipase from Rhizopus chinensis during solid-state fermentation: Biochemical characterization and its esterification potential for ester synthesis

Rhizopus chinensis produces two lipases that catalyze ester synthesis when cultured under solid-state fermentation. The Lip2 was purified to homogeneity by ammonium sulphate precipitation, hydrophobic interaction chromatography and gel filtration chromatography. It has an apparent molecular weight of 33 kDa estimated from SDS–PAGE and 32 kDa calculated from analytical gel permeation, with synthetic activity and purification fold of 96.8 U/mg and 138.3, respectively. Maximum hydrolytic activity was obtained at pH 8.0–8.5 and 40 °C using pNPP as substrate. Slight activation of the enzyme was observed when Mn²⁺ is present. The enzyme was most active on p-nitrophenyl laurate (C12). The purified lipase exhibited maximum synthetic activity at pH memory of 6.0 and 30 ^oC. Most of ethyl esters synthesized by lyophilized enzyme achieved good yields (>90%), and caprylic acid served as the best acyl donor. The enzyme presented a particular affinity for ethanol, n-propanol and n-hexanol, with conversion of 92%, 93% and 92%, respectively, after 20 h incubation.