Synthesis of mixed esters of ascorbic acid using methyl esters of palm and soybean oils

Mixed esters of ascorbic acid were synthesized using methyl esters of palm and soybean oils as acyl donors, in acetone at 50 degrees C, and catalyzed by Novozym 435. A conversion of 62% was obtained with palm oil methyl ester at an ascorbic acid to acyl donor molar ratio of 1:4; the mixed ester contained 45.89% ascorbyl palmitate, 42.59% ascorbyl oleate and 10.1% ascorbyl linoleate. Acylation with soybean oil methyl ester resulted in 17% conversion, yielding a mixed ester containing 10.08% ascorbyl palmitate, 20.68% ascorbyl oleate, and 64.96% of ascorbyl linoleate. The mixed esters of ascorbic acid can find direct use in food and cosmetics.     

Solvent-free glycerolysis of palm and palm kernel oils catalyzed by commercial 1,3-specific lipase from Humicola lanuginosa and composition of glycerolysis products

Glycerolysis of palm and palm kernel oils were conducted using a commercial 1,3-specific lipase from Humicola lanuginosa (trade name: SP 398) as catalyst (500 units lipase g^–1 oil) at 40°C and oil:glycerol (1:2 mol mol^–1) in a solvent-free system. After 24 h, the glycerolysis products of palm and palm kernel oils consisted of 23% triacylglycerols, 18% monoacylglycerols, 38% diacylglycerols and 18% triacylglycerols, 31% monoacylglycerols, 42% diacylglycerols, respectively. The monoacylglycerol fraction of the glycerolysis product of palm oil was enriched in oleic acid. Palmitic acid content of the monoacylglycerol fraction of the same product was less than that of the original oil. Under the same conditions, monacylglycerol fraction of the palm kernel oil glycerolysis product was enriched in palmitic, stearic and oleic acids.     

Secretory expression and characterization of a highly Ca-activated thermostable L2 lipase

Thermostable lipases are important biocatalysts, showing many interesting properties with industrial applications. Previously, a thermophilic Bacillus sp. strain L2 that produces a thermostable lipase was isolated. In this study, the gene encoding for mature thermostable L2 lipase was cloned into a Pichia pastoris expression vector. Under the control of the methanol-inducible alcohol oxidase (AOX) promoter, the recombinant L2 lipase was secreted into the culture medium driven by the Saccharomyces cerevisiae α-factor signal sequence. After optimization the maximum recombinant lipase activity achieved in shake flasks was 125 U/ml. The recombinant 44.5 kDa L2 lipase was purified 1.8-fold using affinity chromatography with 63.2% yield and a specific activity of 458.1 U/mg. Its activity was maximal at 70 °C and pH 8.0. Lipase activity increased 5-fold in the presence of Ca²⁺. L2 lipase showed a preference for medium to long chain triacylglycerols (C₁₀–C₁₆), corn oil, olive oil, soybean oil, and palm oil. Stabilization at high temperature and alkaline pH as well as its broad substrate specificity offer great potential for application in various industries that require high temperature operations.     

Enzymatic synthesis and anti-oxidative activities of plant oil-based ascorbyl esters in 2-methyltetrahydrofuran-containing mixtures

Ascorbyl fatty acid esters are commercially interesting fat-soluble antioxidants. In this work, enzymatic synthesis of ascorbyl esters from less expensive and readily available plant oils, and their anti-oxidative activities are described. Among the immobilized lipases tested, Candida antarctica lipase B was the best for the synthesis of plant oil-based ascorbyl esters. The enzyme showed much better catalytic performances in the binary mixtures of biomass-based 2-methyltetrahydrofuran (MeTHF) and t-butanol than the previously preferred t-butanol. The conversions of 70–73% were obtained under the optimal reaction conditions after 24?h, with the unsaturated fatty acid esters (oleate and linoleate, 80–90%) as the major products. The immobilized lipase kept the relative activity of 80% after reuse for 6 batches in MeTHF-containing system. Besides, anti-oxidative activities of plant oil-based ascorbyl esters and ascorbic acid were comparable, which could remove α,α-diphenyl-β-picrylhydrazyl (DPPH) free radical of >87%.     

Magnetic nanoparticles supported ionic liquids for lipase immobilization: Enzyme activity in catalyzing esterification

Candida rugosa lipase was immobilized on magnetic nanoparticles supported ionic liquids having different cation chain length (C₁, C₄ and C₈) and anions (Cl⁻, BF₄⁻ and PF₆⁻). Magnetic nanoparticles supported ionic liquids were obtained by covalent bonding of ionic liquids–silane on magnetic silica nanoparticles. The particles are superparamagnetic with diameter of about 55 nm. Large amount of lipase (63.89 mg/(100 mg carrier)) was loaded on the support through ionic adsorption. Activity of the immobilized lipase was examined by the catalysis of esterification between oleic acid and butanol. The activity of bound lipase was 118.3% compared to that of the native lipase. Immobilized lipase maintained 60% of its initial activity even when the temperature was up to 80 °C. In addition, immobilized lipase retained 60% of its initial activity after 8 repeated batches reaction, while no activity was detected after 6 cycles for the free enzyme.     

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.     

A hyper-thermostable, alkaline lipase from Pseudomonas sp. with the property of thermal activation

A hyper-thermostable, alkaline lipase from a newly-isolated, mesophilic Pseudomonas sp. was optimal at pH 11 and at 90 °C. It had a half-life of more than 13 h at 90 °C. It was activated by 30% when heated at 90 °C for 2 h. The enzyme had a greater affinity for mustard oil (K _m=40 mg ml^–1) than for olive oil (K _m=140 mg ml^–1).     

Effects of oils and oil-related substrates on the synthetic activity of membrane-bound lipase from Rhizopus chinensis and optimization of the lipase fermentation media

The lipase from filamentous fungi Rhizopus chinensis, as a membrane-bound enzyme, possesses the excellent catalysis ability for esterification and transesterification reactions, and has a good potential in many industrial applications. In order to improve the synthetic activity of the lipase, the effects of oils and oil-related substrates on its production and the fermentation media optimization were investigated. Based on the results, it was suggested that oleic acid could be the important substrate for the lipase production. Among various oils and oil-related substrates, olive oil containing high content of oleic acid was the optimal one for the lipase production. Using orthogonal test and response surface methodology (RSM), the composition of fermentation media was further optimized. The optimized media for lipase synthetic activity and activity yield was composed of peptone 57.94 and 55.58 g L⁻¹, olive oil 21.94 and 22.99 g L⁻¹, maltose 12.91 and 14.34 g L⁻¹, respectively, with K₂HPO₄ 3 g L⁻¹, MgSO₄·7H₂O 5 g L⁻¹ and initial pH 6.0. Under the optimal conditions, the lipase activity and the activity yield were improved 61.5 and 93.4% comparing the results before optimization, respectively. The adequate models obtained had predicted the lipase production successfully.     

Mass production of lipase by fed-batch culture of Pseudomonas fluorescens

Summary High concentration production of an extracellular enzyme, lipase, was achieved by a fed-batch culture of Pseudomonas fluorescens. During the cultivation, temperature, pH and dissolved oxygen concentration wwre maintained at 23°C, 6.5 and 2–5 ppm, respectively. Olive oil was used as a carbon source for microbial growth. To produce lipase effectively the specific feed rate of olive oil had to be maintained in a range of 0.04–0.06 (g oil) · (g dry cell)^-1 · h^-1. The CO₂ evolution rate was monitored to estimate the requirement of olive oil. The ratio of feed rate of olive oil to the CO₂ evolution rate was varied in the range of 20–60 g oil/mol CO₂. The higher value of the ratio accelerated microbial growth, but did not favour lipase production. Once the high cell concentration of 60 g/l had been achieved, the ratio was changed from 50 to 30 g oil/mol CO₂ to accelerate the lipase production. By this CO₂-dependent method a very high activity of lipase, 1980 units/ml, was obtained. Both the productivity and yield of lipase were prominently increased compared with a conventional batch culture.     

Screening Botryosphaeria species for lipases: Production of lipase by Botryosphaeria ribis EC-01 grown on soybean oil and other carbon sources

Nine isolates of Botryosphaeria spp. were screened for lipases when cultivated on eight different plant seed oils and glycerol, and all produced lipases. Botryosphaeria ribis EC-01 produced highest lipase titres on soybean oil and glycerol, while eight isolates of Botryosphaeria rhodina produced significantly lower enzyme titres. B. ribis EC-01 produced lipase when grown on different fatty acids, surfactants, carbohydrates and triacylglycerols, with highest enzyme titres produced on Triton X-100-emulsified stearic (316.7 U/mL), palmitic (283.5 U/mL) and oleic (247.4 U/mg) acids, and soybean oil (105.6 U/mL), as well as castor oil (191.2 U/mg); an enhancement of 9-fold over soybean oil-grown cultures. Glycerol was also a good substrate for lipase production. The crude lipase extract was optimally active at pH 8.0 and 55 °C, stable between 30 and 55 °C and pH 1–10, and tolerant to 50% (v/v) glycerol, methanol and ethanol. The crude lipase showed affinity for substrates of short, average and long-chain fatty acids (different esters of p-nitrophenol and triacylglycerols). Zymograms developed with 4-methylumbelliferyl-butyrate showed two bands of lipolytic activity at 45 and 15 kDa. This is the first report on the production of lipases by B. ribis grown on these different carbon sources.     

Enzymatic pre-hydrolysis applied to the anaerobic treatment of effluents from poultry slaughterhouses

A pool of hydrolases with 21.4 U g⁻¹ lipase activity was produced through solid-state fermentation of the fungus Penicillium restrictum in waste from the Orbignya oleifera (babassu) oil processing industry. Enzymatic hydrolysis and anaerobic biodegradability tests were conducted on poultry slaughterhouse effluents with varying oil and grease contents (150–1200 mg l⁻¹) and solid enzymatic pool concentrations (0.1–1.0% w/v). Enhanced anaerobic treatment efficiency relative to raw effluent was achieved when a 0.1% concentration of enzymatic pool was used in the pre-hydrolysis stage with 1200 mg oil and grease l⁻¹ (chemical oxygen demand (COD) removal efficiency of 85% vs. 53% and biogas production of 175 ml vs. 37 ml after 4 d).     

A newly isolated fungal strain used as whole‐cell biocatalyst for biodiesel production from palm oil

A strain of Aspergillus niger isolated from atmospherically exposed bread and Jatropha curcas seed was utilized as a whole‐cell biocatalyst for palm oil methanolysis to produce fatty acid methyl esters (FAME), or biodiesel. The A. niger strain had a lipase activity of 212.58 mU mL^?1 after 144 h incubation at 25 °C with an initial pH value of 6.5, using 7% polypeptone (w/w on basal medium) as the nitrogen source and 3% olive oil (w/w on basal medium) as a carbon source. The A. niger cells spontaneously immobilized within polyurethane biomass support particles (BSPs) during submerged fermentation. Thereafter, the methanolysis of palm oil was achieved via a three‐step addition of methanol in the presence of BSPs‐immobilized with A. niger cells. The influence of water content, reaction temperature and enzyme concentration on reaction rate was investigated. An 8% water content and a temperature of 40 °C in the presence of 30 immobilized BSPs, resulted in an 87% FAME yield after 72 h.     

Cross-linked enzyme aggregates (CLEAs) with controlled particles: Application to Candida rugosa lipase

Aggregation agent type and concentration, lipase and glutaraldehyde concentration, and pH are able to affect the formation of cross-linked lipase. The carrier-free immobilized Candida rugosa lipase with a particle size of 40–50 μm showed higher activity than that of the lipase with other particle sizes. The carrier-free immobilized C. rugosa lipase can keep 86% original lipase activity (0.018 g g⁻¹ min⁻¹). The enantioselectivity of the carrier-free immobilized lipase (23.3) was about 1.8 times as much as that of the native lipase (13.0) in kinetic resolution of ibuprofen racemic mixture.     

Gene cloning,expression and characterization of a cold-adapted lipase from a psychrophilic deep-sea bacterium Psychrobacter sp. C18

A psychrophilic bacterium Psychrobacter sp. C18 previously isolated from the Southern Okinawa Trough deep-sea sediments showed extracellular lipolytic activity towards tributyrin. A genomic DNA library was constructed and screened to obtain the corresponding lipase gene. The sequenced DNA fragment contains an open reading frame of 945 bp, which was denoted as the lipX gene, from which a protein sequence LipX was deduced of 315 amino acid residues with a molecular mass of 35,028 Da. This protein contained the bacterial lipase GNSMG (GxSxG, x represents any amino acid residue) and HG consensus motifs. The recombinant pET28a(+)/lipX gene was overexpressed in heterologous host Escherichia coli BL21 (DE3) cells to overproduce the lipase protein LipX_His with a 6× histidine tag at its C-terminus. Nickel affinity chromatography was used for purification of the expressed recombinant lipase. The maximum lipolytic activity of the purified recombinant lipase was obtained at temperature of 30°C and pH 8.0 with p-nitrophenyl myristate (C14) as a substrate. Thermostability assay indicated that the recombinant LipX_His is a cold-adapted lipase, which was active in 10% methanol, ethanol, acetone and 30% glycol, and inhibited partially by Zn²⁺, Co²⁺, Mn²⁺, Fe³⁺ and EDTA. Most non-ionic detergents, such as DMSO, Triton X-100, Tween 60 and Tween 80 enhanced the lipase activity but 1% SDS completely inhibited the enzyme activity. Additionally, the highest lipolytic rate of the recombinant LipX_His lipase was achieved when p-nitrophenyl myristate was used as a substrate, among all the p-nitrophenyl esters tested.     

Biocatalytic acylation of carbohydrates with fatty acids from palm fatty acid distillates

Palm fatty acid distillates (PFAD) are by-products of the palm oil refining process. Their use as the source of fatty acids, mainly palmitate, for the biocatalytic synthesis of carbohydrate fatty acid esters was investigated. Esters could be prepared in high yields from unmodified acyl donors and non-activated free fatty acids obtained from PFAD with an immobilized Candida antarctica lipase preparation. Acetone was found as a compatible non-toxic solvent, which gave the highest conversion yields in a heterogeneous reaction system without the complete solubilization of the sugars. Glucose, fructose, and other acyl acceptors could be employed for an ester synthesis with PFAD. The synthesis of glucose palmitate was optimized with regard to the water activity of the reaction mixture, the reaction temperature, and the enzyme concentration. The ester was obtained with 76% yield from glucose and PFAD after reaction for 74 h with 150 U ml⁻¹ immobilized lipase at 40°C in acetone.     

Physical and stability characteristics of Burkholderia cepacia lipase encapsulated in κ-carrageenan

In this work, a novel approach for lipase immobilization was exploited. Lipase from Burkholderia cepacia was encapsulated into κ-carrageenan by co-extrusion method to form a liquid core capsule. The diameter of the encapsulated lipase was found to be in the range of 1.3–1.8 mm with an average membrane thickness of 200 μm and 5% coefficient of variance. The encapsulation efficiency was 42.6% and 97% moisture content respectively. The encapsulated lipase was stable between pH 6 and 9 and temperature until 50 °C. The encapsulated lipase was stable until disintegration of the carrier when stored at 27 °C and retained 72.3% of its original activity after 6 cycles of hydrolysis of p-NPP. The encapsulated lipase was stable in various organic solvents including methanol, ethanol, iso-propanol, n-hexane and n-heptane. Kinetic parameters K_m and V_max were found to be 0.22 mM and 0.06 μmol/min for free lipase and 0.25 mM and 0.05 μmol/min for encapsulated lipase respectively.     

Acid hydrolysis of sugarcane bagasse for lactic acid production

In order to use sugarcane bagasse as a substrate for lactic acid production, optimum conditions for acid hydrolysis of the bagasse were investigated. After lignin extraction, the conditions were varied in terms of hydrochloric (HCl) or sulfuric (H₂SO₄) concentration (0.5–5%, v/v), reaction time (1–5 h) and incubation temperature (90–120 °C). The maximum catalytic efficiency (E) was 10.85 under the conditions of 0.5% of HCl at 100 °C for 5 h, which the main components (in g l⁻¹) in the hydrolysate were glucose, 1.50; xylose, 22.59; arabinose, 1.29; acetic acid, 0.15 and furfural, 1.19. To increase yield of lactic acid production from the hydrolysate by Lactococcus lactis IO-1, the hydrolysate was detoxified through amberlite and supplemented with 7 g l⁻¹ of xylose and 7 g l⁻¹ of yeast extract. The main products (in g l⁻¹) of the fermentation were lactic acid, 10.85; acetic acid, 7.87; formic acid, 6.04 and ethanol, 5.24.     

An integrated approach to produce biodiesel and monoglycerides by enzymatic interestification of babassu oil (Orbinya sp)

Two screenings of commercial lipases were performed to find a lipase with superior performance for the integrated production of biodiesel and monoglycerides. The first screening was carried out under alcoholysis conditions using ethanol as acyl acceptor to convert triglycerides to their corresponding ethyl esters (biodiesel). The second screening was performed under glycerolysis conditions to yield monoglycerides (MG). All lipases were immobilized on silica–PVA composite by covalent immobilization. The assays were performed using babassu oil and alcohols (ethanol or glycerol) in solvent free systems. For both substrates, lipase from Burkholderia cepacia (lipase PS) was found to be the most suitable enzyme to attain satisfactory yields. To further improve the process, the Response Surface Methodology (RSM) was used to determine the optima operating conditions for each biotransformation. For biodiesel production, the highest transesterification yield (>98%) was achieved within 48 h reaction at 39 °C using an oil-to-ethanol molar ratio of 1:7. For MG production, optima conditions corresponded to oil-to-glycerol molar ratio of 1:15 at 55 °C, yielding 25 wt.% MG in 6 h reaction. These results show the potential of B. cepacia lipase to catalyze both reactions and the feasibility to consider an integrated approach for biodiesel and MG production.     

The ascorbic acid content of eleven species of microalgae used in mariculture

The ascorbic acid (vitamin C) concentrations in 11 species of microalgae commonly used in mariculture were determined. The species examined were 4 diatoms (Chaetoceros calcitrans (Paulsen) Takano,Chaetoceros gracilis Schütt,Skeletonema costatum (Greville) Cleve,Thalassiosira pseudonana (Hustedt, clone 3H) Hasle and Heimdal); 2 prymnesiophytes (Isochrysis sp. (clone T.ISO) Parke,Pavlova lutheri (Droop) Green); 1 prasinophyte (Tetraselmis suecica (Kylin) Butcher); 2 chlorophytes (Dunaliella tertiolecta Butcher,Nannochloris atomus Butcher); 1 eustigmatophyte (Nannochloropsis oculata (Droop) Green); and 1 cryptophyte (Chroomonas salina (Wislouch) Butcher). Duplicate cultures of each species were grown under defined conditions and analysed during both logarithmic and stationary phase of growth.Average values for ascorbic acid ranged from 9.4 fg cell^–1 (N. oculata, stationary phase) to 700 fg cell^–1 (S. costatum, stationary phase). This value was generally related to cell size. Levels of ascorbic acid cell^–1 increased during the stationary growth phase forS. costatum andD. tertiolecta and decreased forC. gracilis, T. pseudonana, C. salina andN. oculata. Levels did not change significantly for the remaining species.Average values for per cent ascorbic acid ranged from 0.11% (T. pseudonana, stationary phase) to 1.62% of dry weight (C. gracilis, logarithmic phase). The per cent ascorbic acid was not related to algal class. Also, the percentage between logarithmic and stationary phase cultures differed for many of the species, but differences were unrelated to algal class.Chaetoceros gracilis, T. pseudonana, N. oculata andIsochrysis sp. (T.ISO) had higher per cent ascorbic acid during the logarithmic phase, whereasD. tertiolecta andN. atomus contained more per cent ascorbic acid during the stationary phase.Despite the differences in the composition of the different microalgae (0.11–1.62% ascorbic acid), all species would provide a rich source of ascorbic acid for maricultured animals, which can require 0.003–0.02% of the vitamin in their diet.     

Production of structured triacylglycerols by acidolysis catalyzed by lipases immobilized in a packed bed reactor

The aim of this work was to produce structured triacylglycerols (STAGs), with caprylic acid located at positions 1 and 3 of the glycerol backbone and docosohexaenoic acid (DHA) at position 2, by acidolysis of tuna oil and caprylic acid (CA) catalyzed by lipases Rd, from Rhizopus delemar, and Palatase 20000L from Mucor miehei immobilized on Accurel MP1000 in a packed bed reactor (PBR), working in continuous and recirculation modes. First, different lipase/support ratios were tested for the immobilization of lipases and the best results were obtained with ratios of 0.67 (w/w) for lipase Rd and 6.67 (w/w) for Palatase. Both lipases were stable for at least 4 days in the operational conditions. In the storage conditions (5 °C) lipases Rd and Palatase maintained constant activity for 5 months and 1 month, respectively.These catalysts have been used to obtain STAGs by acidolysis of tuna oil and CA in a PBR operating with recirculation of the reaction mixture through the lipase bed. Thus, STAGs with 52–53% CA and 14–15% DHA were obtained. These results were the basis for establishing the operational conditions to obtain STAGs operating in continuous mode. These new conditions were established maintaining constant intensity of treatment (IOT, lipase amount × reaction time/oil amount). In this way STAGs with 44–50% CA and 17–24% DHA were obtained operating in continuous mode. Although the compositions of STAGs obtained with both lipases were similar, Palatase required an IOT about four times higher than lipase Rd.To separate the acidolysis products (free fatty acids, FFAs, and STAGs) an extraction method of FFAs by water–ethanol solutions was tested. The following variables were optimized: water/ethanol ratio (the best results were attained with a water/ethanol ratio of 30:70, w/w), the solvent/FFA–STAG mixture ratio (3:1, w/w) and the number of extraction steps (3–5). In these conditions highly pure STAGs (93–96%) were obtained with a yield of 85%. The residual FFAs can be eliminated by neutralization with a hydroethanolic KOH solution to obtain pure STAGs. The positional analysis of these STAGs, carried out by alcoholysis catalyzed by lipase Novozym 435, has shown that CA represents 55% of fatty acids located at positions 1 and 3 and DHA represents 42% of fatty acids at position 2.