Kinetics modeling of the acidolysis with immobilized Rhizomucor miehei lipases for production of structured lipids from sunflower oil

Sunflower oil modification for production of semisolid fats was carried out via acidolysis using palmitic and stearic acids (P + St), hexane and a developed biocatalyst from Rhizomucor miehei lipases. Its kinetic behavior was studied by employing three mathematical models proposed in the literature. Furthermore, a new model was proposed to describe not only the variation of triacylglycerols (TAG), diacylglycerols (DAG), and free fatty acids groups but also the acyl migration reaction occurrence. The effect of the reaction temperature on the kinetic and equilibrium parameters, as well as TAG and reaction intermediates profiles was analyzed. Increasing reaction temperature generated major changes in the overall composition of acylglycerols and gave rise to the highest composition of P + St in the obtained structured lipids (58%, 70 h, 60 °C). P + St incorporation was successfully adjusted by an empirical model (Model I) and a lumped parameter model (Model II) for all the studied reaction times, while the model based on a Ping Pong Bi Bi mechanism (Model III) was only able to describe the kinetics behavior (through the variation of reactant saturated fatty acids concentration) until 24 h. Experimental data were fit satisfactorily by the proposed model (Model IV), showing that the increment in the disaturated TAG formation achieved by the increment in temperature was principally related to the favored DAG formation from triunsaturated TAG.     

Synthesis of structured lipids by two enzymatic steps: Ethanolysis of fish oils and esterification of 2-monoacylglycerols

This paper studies the synthesis of structured triacylglycerols (STAGs), rich in polyunsaturated fatty acids (PUFAs) by a two-step enzymatic process: (i) alcoholysis of fish oils (cod liver and tuna oils) with ethanol to obtain 2-monoacylglycerols (2-MAGs), catalyzed by 1,3 specific lipases and (ii) esterification of these 2-MAGs with caprylic acid (CA, 8:0), also catalyzed by a 1,3 specific lipase, to produce STAGs of structure CA–PUFA–CA. As regards the alcoholysis reaction, three factors have been studied: the influence of the type of lipase used (lipase D from Rhizopus oryzae, immobilized on Accurel MP1000, and Novozym 435 from Candida antarctica), the operational mode of a stirred tank reactor (STR operating in discontinuous and continuous mode) and the intensity of treatment (IOT = lipase amount × reaction time/oil amount). Although higher 2-MAG yields were obtained with lipase D, Novozym 435 was selected due to its greater stability in the operational conditions. The highest 2-MAG yield (63%) was attained in the STR operating in discontinuous mode at an IOT of 1 g lipase × h g oil^?1 (at higher IOT the 2-MAGs were degraded to glycerol). This system was scaled up to 100 times the initial volume, achieving a similar yield (65%) at the same IOT. The 2-MAGs in the final alcoholysis reaction mixture were separated from ethyl esters by solvent extraction using solvents of low toxicity (ethanol and hexane); the 2-MAG recovery yield was over 90% and the purity was approximately 87–90%. Regarding the esterification of the 2-MAGs, the following factors were studied: the influence of the lipase type used, the presence or absence of solvent (hexane) and the reaction time or intensity of treatment (IOT = lipase amount × reaction time/2-MAG amount). Of the five lipases tested, the highest STAG percentages (over 90%) were attained with lipases D and DF, immobilized on Accurel MP1000. These STAGs contain 64% CA, of which 98% is at positions 1 and 3. Position 2 contains 5% CA and 45% PUFAs, which means that all the PUFAs that were located at position 2 in the original oil remain in that position in the final STAGs. The lipase D immobilized on Accurel MP1000 is stable in the operational conditions used in the esterification reaction. Finally the purification of STAGs was carried out by neutralization of free fatty acids with hydroethanolic solution of KOH and extraction of STAGs with hexane. By this method purity was over 95% and separation yields were about 80%.     

Production of triacylglycerols rich in palmitic acid at position 2 as intermediates for the synthesis of human milk fat substitutes by enzymatic acidolysis

This paper studies the synthesis of triacylglycerols (TAGs) rich in palmitic acid (PA) at position 2, from palm oil stearin (POS), a vegetable oil highly rich in this acid (60%). The developed process consists of two steps: (1) obtaining PA enriched free fatty acids (FFAs), and (2) enrichment of POS in PA by acidolysis of this oil with PA enriched FFAs, catalyzed by lipase Novozym 435. In step (1) two PA enriched FFA mixtures were obtained: one by saponification of POS, and a PA concentrate (75.1% PA) obtained by crystallization at low temperature in solvents. The latter was obtained carrying out two crystallizations in acetone at −24 and −20 °C, from which PA was recovered in the solid phases with a total yield of 84%. These PA enriched FFA mixtures were used in step (2) of acidolysis of POS, along with commercial PA (98% PA). In this acidolysis step four factors were studied: temperature, hexane/reaction mixture ratio, FFA/POS molar ratio and the intensity of treatment (IOT = lipase amount × reaction time/POS amount). The best results (TAGs with 79% PA and 75% PA at position 2) were obtained with commercial PA, at 37 °C, 10 mL hexane/g reaction mixture, a FFA/POS molar ratio 3:1 (1:1, w/w) and an IOT = 9.6 g lipase × h/g POS (for example 48 h, 10 g lipase and 50 g POS). PA enriched TAGs were purified neutralizing the FFAs by KOH hydroethanolic solutions and extracting the TAGs with hexane. In this way 99% pure acylglycerols (TAG + DAG) were obtained; the recovery yield of this purification step was 95%. The experiments carried out with POS demonstrated that it is possible to use only this oil (60% PA, 23% PA at position 2) as a source of PA to obtain a TAG with 70.7% PA and 70.5% PA at position 2. This process consists of four steps: (1) saponification of POS, (2) crystallization of FFAs to obtain PA enriched FFAs (75.1% PA), (3) acidolysis of POS with these FFAs, catalyzed with Novozym 435, to produce PA enriched TAGs at position 2 (70.5% PA) and (4) purification of TAGs to obtain approximately 95% purity and yield. These PA enriched TAGs could be used to obtain structured TAGs rich in PA at position 2 and in oleic acid at positions 1 and 3 (OPO), which is the principal TAG of human milk fat.     

Expanded bed adsorption of an alkaline lipase from Pseudomona cepacia

An extracellular lipase was isolated from Pseudomona cepacia by expanded bed adsorption on an Amberlite 410 ion-exchange resin. Enzyme characterization and hydrodynamic study of a chromatography column were done. Enzyme purification was done at three condition of expanded bed height (H): at one and half (6 cm), at two (8 cm) and at three (12 cm) times the fixed bed height (H₀ = 4 cm). The results showed that the experimental data was fitted to the Richardson and Zaki equation, and the comparison between the experimental and calculated terminal velocities showed low relative error. In enzyme purification for better condition, a purification factor of about 80 times was found at 6 cm of expanded bed height, or 1.5 times of expansion degree. Purified lipase had an optimal pH and a temperature of 8 and 37 °C, respectively.     

Immobilization of acidic lipase derived from Pseudomonas gessardii onto mesoporous activated carbon for the hydrolysis of olive oil

Mesoporous activated carbon (MAC) derived from rice husk is used for the immobilization of acidic lipase (ALIP) produced from Pseudomonas gessardii. The purified acidic lipase had the specific activity and molecular weight of 1473 U/mg and 94 kDa respectively. To determine the optimum conditions for the immobilization of lipase onto MAC, the experiments were carried out by varying the time (10–180 min), pH (2–8), temperature (10–50 °C) and the initial lipase activity (49 × 10³, 98 × 10³, 147 × 10³ and 196 × 10³ U/l in acetate buffer). The optimum conditions for immobilization of acidic lipase were found to be: time—120 min; pH 3.5; temperature—30 °C, which resulted in achieving a maximum immobilization of 1834 U/g. The thermal stability of the immobilized lipase was comparatively higher than that in its free form. The free and immobilized enzyme kinetic parameters (K_m and V_max) were found using Michaelis–Menten enzyme kinetics. The K_m values for free enzyme and immobilized one were 0.655 and 0.243 mM respectively. The immobilization of acidic lipase onto MAC was confirmed using Fourier Transform-Infrared Spectroscopy, X-ray diffraction analysis and scanning electron microscopy.     

Enzymatic synthesis of fatty acid methyl esters from lard with immobilized Candida sp. 99-125

In this paper, immobilized lipase catalyzed biodiesel production from lard was studied. Using Candida sp. 99-125, the effect of temperature, water content, enzyme amount, solvent and three-step methanolysis were investigated. The optimal conditions for processing 1 g of lard were: 0.2 g immobilized lipase, 8 ml n-hexane as solvent, 20% water based on the fat weight, temperature 40 °C, and three-step addition of methanol. As a result, the fatty acid methyl esters (FAMEs) yield was 87.4%. The lipase was proved to be stable when used repeatedly for 180 h.     

Fatty acid production from butter using novel cutinase-displaying yeast

We used cutinase from the filamentous fungi Aspergillus oryzae to produce dairy flavors. Secretory and displayed forms of cutinase were investigated using salt-free butter, which is composed mostly of triacylglycerides, as the substrate. The secretory form of cutinase, which was produced in recombinant A. oryzae, was suitable for producing butyric acids (16.8 mol%). Also, cutinase displayed on the cell surface of the yeast Saccharomyces cerevisiae as a fusion protein with α-agglutinin released butyric acid at a 2.7-fold rate (45.4 mol%) higher than that of the secreted form. Yeasts carrying two copies of cutinase genes into their chromosomes, which were constructed using the HELOH method, released free fatty acids rapidly and showed 2-fold higher lipase activity compared with yeasts carrying one copy of the cutinase gene.     

The age of monumental olive trees (Olea europaea) in northeastern Spain

Trees can reach ages that in some cases amount to thousands of years. In the Mediterranean region, olive trees (Olea europaea) have traditionally been considered a particularly long-lived species. The main objective of this study was to assess the age of large olive trees considered to be millenarian and classified as monumental trees in northeastern Spain. We extracted cores of 14 individuals and obtained 8 sections of trees which had already been cut in the area where the largest olive trees in the northeastern Iberian Peninsula are found. The age of the sampled olive trees was assessed by counting the number of annual growth rings. Tree rings did not cross-date well, neither within nor between individuals, but boundaries between likely annual rings were clearly distinct. We found a linear relationship between DBH and tree age (in years) (Age = 2.11 × diameter(cm) + 88.93, R² = 0.80), which was used to estimate the age of unsampled olive trees. The maximum estimated age (627 ± 110 years) is among the greatest ages reported for olive trees around the world (700 years) and among the oldest trees in Mediterranean ecosystems.     

Directed bioconversion of Kraft lignin to polyhydroxyalkanoate by Cupriavidus basilensis B-8 without any pretreatment

This work presents here a new fundamental strategy for bio-converting Kraft lignin (KL) into useful products. Cupriavidus basilensis B-8 (here after B-8) was able to use KL as the sole carbon source. Fully 41.5% of lignin, 37.7% of total carbon (TC) and 43.0% of color were removed after 7 days of incubation. At the same time, lignin was depolymerized into small fragments, which was confirmed by scanning electron microscopy (SEM) and gel permeation chromatography (GPC). Bacterial biomass accumulated to 735.6 mg/L at the initial KL concentration of 5 g L⁻¹, and the corresponding volumetric productivity of polyhydroxyalkanoate (PHA) was 128 mg/L. PHA productivity was significantly improved through fed batch fermentation and reached to 319.4 mg/L. GC–MS analysis showed that PHA polymer was composed of three basic monomers: 98.3 mol% of (S)-3-hydroxy-butanoic acid (S3HB), 1.3 mol% of ^®-3-hydroxybutyric acid (R3HB) and 0.4 mol% of 3-hydroxy-butanoic acid (3HB).     

Transluminal attenuation-gradient coronary CT angiography on a 320-MDCT volume scanner: Effect of scan timing,coronary artery stenosis,and cardiac output using a contrast medium flow phantom

PurposeTransluminal-attenuation-gradient (TAG) may reflect patient characteristics and physiological parameters. Furthermore, TAG may be affected by factors such as the CT scanner speed, scanning method, scan timing after contrast-medium (CM) injection, and the injection methods. The purpose of our study was to investigate quantitative TAG at different scan timing points after CM injection for coronary CT angiography.Materials and methodsUsing a CM flow phantom and two types of connecting tube mimicking 0% and 70% coronary artery stenosis, we performed 320-detector volume scanning. The heart rate was set at 60 bpm and cardiac-output (CO) at 2.0 and 4.0 l/min, respectively. The acquisition time repeated at 0.5-s intervals for 40 and 25 s at a CO of 2.0- and 4.0 l/min. We measured the CT number on the same slice level, calculated the time-density-curve (TDC) and the TAG at each time point.ResultsAt COs of 2.0 and 4.0 l/min at 0% stenosis, TAG exhibited smaller variations (−3.02 to +0.55 HU/cm at 2.0 l/min, −2.63 to +0.43 HU/cm at 4.0 l/min) than at 70% stenosis at each time point along the TDC. Compared with a CO at 2.0 l/min with 70% stenosis, the TAG curve for a CO at 4.0 l/min gradually changed with time (−6.64 to +1.18 HU/cm at 2.0 l/min vs. −3.46 to +2.75 HU/cm at 4.0 l/min).ConclusionThe TAG value was affected by scan timing after CM injection and by CO although the size of the connecting tube with and without stenosis was identical.     

Stabilization of sphingomyelin interactions by interfacial hydroxyls — A study of phytosphingomyelin properties

D-ribo-phytosphingosines are biologically significant long-chain bases present in various sphingolipids from yeasts, fungi, plants and mammals. In this study we prepared phytopalmitoylsphingomyelin (phytoPSM) analogs based on the D-ribo-phytosphingosine base. The N-linked acyl chains were either 16:0, 2OH(R)16:0 (natural isomer), or 2OH(S)16:0. The gel-phase of phytoPSM was more stable than that of PSM (T_m 48.6 °C and 41.0 °C, respectively). The gel-liquid crystalline phase transition enthalpies were 9.1 ± 0.4 and 6.1 ± 0.3 kcal/mol for phytoPSM and PSM, respectively. An N-linked 2OH(R)16:0 in phytoPSM destabilized the gel phase relative to phytoPSM (by ~+ 6 °C, based on DPH anisotropy measurements), whereas 2OH(S)16:0 in phytoPSM stabilized it (by ~? 6 °C). All phytoPSM analogs formed sterol-enriched ordered domains in a fluid ternary bilayer, and those containing phytoPSM or 2OH(S)phytoPSM were more thermostable than the domains containing 2OH(R)phytoPSM or PSM. The affinity of cholestatrienol for POPC bilayers containing 20 mol% phytoPSM was higher than for comparable bilayers with an equal amount of PSM. The 2-hydroxylated acyl chains in phytoPSM did not markedly alter sterol affinity. We conclude that phytoPSM is a more ordered sphingolipid than PSM, and is fully capable of interacting with cholesterol.     

Thermophilic lipase from Thermomyces lanuginosus: Gene cloning,expression and characterization

An extracellular lipase gene ln1 from thermophilic fungus Thermomyces lanuginosus HSAUP₀₃80006 was cloned through RT-PCR and RACE amplification. Its coding sequence predicted a 292 residues protein with a 17 amino acids signal peptide. The deduced amino acids showed 78.4% similarity to another lipase lgy from T. lanuginosus while shared low similarity with other fungi lipases. Higher frequencies hydrophobic amino acids related to lipase thermal stability, such as Ala, Val, Leu and Gly were observed in this lipase (named LN). The sequence, -Gly-His-Ser-Leu-Gly-, known as a lipase-specific consensus sequence of mould, was also found in LN. High level expression for recombinant lipase was achieved in Pichia pastoris GS115 under the control of strong AOX1 promoter. It was purified to homogeneity through only one step DEAE-Sepharose anion exchange chromatography and got activity of 1328 U/ml. The molecular mass of one single band of this lipase was estimated to be 33 kDa by SDS-PAGE. The enzyme was stable at 60 °C and kept 65% enzyme activity after 30 min incubation at 70 °C. It kept half-activity after incubated for 40 min at 80 °C. The optimum pH for enzyme activity was 9.0 and the lipase was stable from pH 8.0 to 12.0. Lipase activity was enhanced by Ca²⁺ and inhibited by Fe²⁺, Zn²⁺, K⁺, and Ag⁺. The cell-free enzyme hydrolyzed and synthesized esters efficiently, and the synthetic efficiency even reached 81.5%. The physicochemical and catalytic properties of the lipase are extensively investigated for its potential industrial applications.     

Esterification activity and stability of Talaromyces thermophilus lipase immobilized onto chitosan

The Talaromyces thermophilus lipase (TTL) was immobilized by different methods namely adsorption, ionic binding and covalent coupling, using various carriers. Chitosan, pre-treated with glutaraldehyde, was selected as the most suitable support material preserving the catalytic activity almost intact and offering maximum immobilization capacity (76% and 91%, respectively). The chitosan-immobilized lipase could be reputably used for ten cycles with more than 80% of its initial hydrolytic activity. Shift in the optimal temperature from 50 to 60 °C and in the pH from 9.5 to 10, were observed for the immobilized lipase when compared to the free enzyme.The catalytic esterification of oleic acid with 1-butanol has been carried out using hexane as organic solvent. A high performance synthesis of 1-butyl oleate was obtained (95% of conversion yield) at 60 °C with a molar ratio of 1:1 oleic acid to butanol and using 100 U (0.2 g) of immobilized lipase. The esterification product is analysed by GC/MS to confirm the conversion percentage calculated by titration.     

Ethyl isovalerate synthesis using Candida rugosa lipase immobilized on silica nanoparticles prepared in nonionic reverse micelles

Uniform and monodispersed silica nanoparticles were synthesized with a mean diameter of 100 ± 20 nm as analyzed by Transmission Electron Microscopy (TEM). Glutaraldehyde was used as a coupling agent for efficient binding of the lipase onto the silica nanoparticles. For the hydrolysis of pNPP at pH 7.2, the activation energy within 25–40 °C for free and immobilized lipase was 7.8 and 1.25 KJ/mol, respectively. The V_max and K_m of immobilized lipase at 25 °C for pNPP hydrolysis were found to be 212 μmol/min/mg and 0.3 mM, whereas those for free lipase were 26.17 μmol/min and 1.427 mM, respectively. The lower activation energy of immobilized lipase in comparison to free lipase suggests a change in conformation of the enzyme leading to a requirement for lower energy on the surface of the nanoparticles. A better yield (7 fold higher) of ethyl isovalerate was observed using lipase immobilized onto silica nanoparticles in comparison to free lipase.     

Tween 80 influences the production of intracellular lipase by Schizochytrium S31 in a stirred tank reactor

Marine microorganisms are a potential source of enzymes with structural stability, high activity at low temperature and unique substrate selectivity. Thraustochytrids are marine heterotrophic microbes, well known for the production of omega-3 fatty acids. In this study the effect of Tween 80 as a carbon source was investigated with regard to biomass, lipase and lipid productivity in Schizochytrium sp. S31. Tween 80 (1%) and 120 h of incubation were the optimum condition period for biomass, lipid and lipase productivity in a stirred tank reactor. The yields obtained were 0.9 g L⁻¹ of biomass, 300 mg g⁻¹ of lipid and 39 U/g of lipase activity. Sonication was optimised in terms of time and acoustic power to maximise the yield of extracted lipase. The extracted lipase from Schizochytrium S31 was observed to hydrolyse long chain polyunsaturated fatty acids DHA and EPA.     

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.     

Resorcinolic lipids improve the properties of sphingomyelin–cholesterol liposomes

Alkylresorcinolic lipids isolated from cereal grains and their semi-synthetic myristoyl-sulphonyl derivatives (MSAR) were used to modify small long-circulating sphingomyelin–cholesterol liposomes. Those SM:Chol vesicles modified with 10–30 mol% resorcinolic lipids had stable size and low membrane permeability in vitro at 4 °C and 37 °C. Liposomes containing 30 mol% MSAR showed very fast solute release in the presence of human plasma at 37 °C, which was drastically diminished in heat-inactivated plasma. In vivo studies showed that unmodified SM:Chol liposomes and those modified with alkylresorcinols were eliminated from the circulation more slowly than liposomes with the highest concentration of MSAR in membrane and were located mostly in the liver and spleen.     

Validation of a simple,rapid and cost effective method for the estimation of caprylic acid and sodium caprylate from biological products using NEFA-C kit

The method for the determination of caprylic acid and sodium caprylate from biological products was systematically validated using NEFA-C kit. The results obtained demonstrated that the kit method was simple, rapid, reliable, sensitive, reproducible and cost effective in comparison to the current methods i.e. colorimetric, High Performance Liquid Chromatography (HPLC) and Gas Chromatography (GC) methods. The assay exhibited excellent linearity, accuracy, precision and robustness. Mean recoveries ranged between 95 and 101.3% (n = 6). The proposed method was linear over the concentration range of 0.05–10 mM of caprylate with values of coefficient of regression being >0.99. Method showed sensitivity of 0.05 mM (7.21 μg/ml for caprylic acid and 8.31 μg/ml for sodium caprylate). The % Relative standard Deviation (%RSD) for intra and interprecision studies was less than 5%. In conclusion the validated method was successfully used in monitoring of processed bulk and final products generated during production of biological products thus laying emphasis on strict control of release criteria for biological products fractionated using caprylic acid.     

A new thermostable and organic solvent-tolerant lipase from Aneurinibacillus thermoaerophilus strain HZ

A thermostable and organic solvent-tolerant lipase produced by Aneurinibacillus thermoaerophilus strain HZ was purified and characterised. The lipase was purified to apparent homogeneity with two steps: anion exchange chromatography on Q-Sepharose and gel filtration on Sephadex-G75. A final specific activity of 43.5 U/mg was obtained with an overall recovery of 19.7% and 15.6 purification fold. The molecular mass of the HZ lipase was estimated to be 50 kDa. The optimum pH for the activity of the purified HZ lipase was 7.0. The stability showed a broad range of pH values between pH 4.0 and 9.0 at 30 °C. The purified HZ lipase exhibited an optimum temperature of 65 °C with a half-life of 3 h and 10 min at 65 °C. The activity of the purified HZ lipase was stimulated in the presence of Ca²⁺. Organic solvents such as dimethyl sulfoxide (DMSO), methanol, n-tetradecane and n-hexadecane enhanced the lipase activity. Studies on the effect of oil showed that the lipase preferred natural oil, such as sunflower oil, over synthetic substrates.     

Screening of lipases for production of novel structured lipids from single cell oils

Lipids enriched in polyunsaturated fatty acids are very susceptible to oxidation, causing the formation of potentially harmful oxidized products. Hence, it is critical to keep the temperature as low as possible during reaction and storage. In this study, five commercial immobilized lipases were evaluated for their capability to produce novel structured lipids (SLs) enriched with medium-chain fatty acids (MCFAs) through acidolysis of single cell oil (SCO) with capric acid. Among the examined lipases, NS40086 and Lipozyme RM IM showed the highest incorporation degree. The acidolysis reactions resulted in an obvious variation in the fatty acids composition as well as their positional distribution. The obtained SLs contained (33.58 %–34.09 %) capric acid at sn-1, 3 positions with increasing the content of arachidonic acid at the sn-2 position up to (49.82 %–50.25 %). The NS40086 lipase displayed 1, 3 regiospecificity towards the TAG of SCO. The acidolysis reactions using NS40086 lipase resulted in a generation of 23 TAG molecular species containing capric acid. Moreover, the NS40086 lipase was more active than Lipozyme RM IM at relatively low temperatures (35 °C and 40 °C), which could be used effectively as a promising biocatalyst in lipid synthesis.