Enzymatic purification of dihomo-γ-linolenic acid from Mortierella single-cell oil

Purification of dihomo-γ-linolenic acid (20:3n−6; DGLA) from a single-cell oil containing 39 wt.% DGLA was attempted. The process comprised: (i) non-selective hydrolysis of the oil to prepare a mixture of free fatty acids (FFAs); (ii) urea adduct fractionation of the FFA mixture to remove saturated fatty acids; and (iii) repeated selective esterification of the resulting mixture with two kinds of lipases. In the first step, Candida rugosa lipase (Lipase-OF from Meito Sangyo Co. Ltd., Aichi, Japan) was the most effective for preparation of the FFAs from the oil; 99% hydrolysis was achieved by the reaction at 40 °C for 72 h. Urea adduct fractionation of the FFA mixture removed almost completely behenic and lignoceric acids, and the content of DGLA increased from 39 to 55 wt.%. The FFAs were esterified with 2 mol equivalent of lauryl alcohol (LauOH) using C. rugosa lipase (Lipase-AY from Amano Enzyme Inc., Aichi, Japan). In consequent, DGLA was enriched to 86 wt.% in the unesterified FFA fraction. To further increase the content of DGLA, the esterification was repeated using the same lipase. Accordingly, the content of DGLA increased to 91 wt.%, but the preparation was contaminated with 3.3 wt.% γ-linolenic acid. This contaminant was removed finally by selective esterification of the FFAs with 2 mol equivalent of LauOH using Pseudomonas aeruginosa lipase. A series of procedures purified DGLA to 95 wt.% in a yield of 51% of the initial content in the single-cell oil.     

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 structured triacylglycerols (STAG) rich in docosahexaenoic acid (DHA) in position 2 by acidolysis of tuna oil catalyzed by lipases

This work deals with the production of structured triacylglycerols (STAG) with caprylic acid (CA) located in positions 1 and 3 of the molecule of glycerol and docosahexaenoic acid (DHA) in position 2, by acidolysis of tuna oil and CA, catalyzed by several lipases. To this end several lipases and immobilization supports were tested with the aim of avoiding the acyl-migration observed in previous works. The determination of the best catalyst (i.e. the lipase and the immobilization support as a whole) was carried out by experiments of acidolysis of cod liver oil and CA in a bath reactor. The best results were obtained with the lipases from Rhizopus oryzae (Lipase D) and Rhizopus delemar (Lipase Rd), immobilized on Accurel MP1000 (a microporous polypropylene) with a lipase/support ratio 1:1.5 (w/w). The activity of these immobilized lipases was stable for a minimum of 5 days in the operational conditions (up to 40 °C).Lipase Rd was selected for the next step in which it was immobilized on Acurrel MP1000 to obtain STAG enriched in DHA by acidolysis of tuna oil (20% DHA) with CA. The experiments were carried out by recirculating the reaction mixture through an immobilized lipase packed bed reactor at different substrate/hexane ratios, as well as in absence of solvent. In the latter case, STAG with 51% CA and 13% DHA were obtained at 73 h. This result indicates that with this catalyst an acceptable reaction rate was attained in absence of solvent. A structural analysis by the pancreatic lipase method carried out to STAG with 45% CA and 16% DHA indicated that 91% of the CA incorporated is located in positions 1 and 3, and that 51% of the DHA is located in position 2 (MLM structure). This position is also rich in palmitic, eicosapentaenoic and oleic acids.After the acidolysis reaction a mixture of STAG and free fatty acids was obtained. The recovery of STAG from this reaction mixture is difficult because of the high content of free fatty acids. A separation method based on the neutralization of the free fatty acids with a KOH hydroalcoholic solution has been developed. By this procedure pure (100%) STAG were obtained with a recovery yield of 80%.     

Optimization of medium chain length fatty acid incorporation into olive oil catalyzed by immobilized Lip2 from Yarrowia lipolytica

Triacylglycerols (TAG) enriched with medium chain fatty acids (M) present specific nutritional, energetic and pharmaceutical properties. Structured lipids (SL) were produced by acidolysis between virgin olive oil and caprylic (C8:0) or capric (C10:0) acids in solvent-free media, catalyzed by the main extracellular lipase from Yarrowia lipolytica lipase 2 (YLL2), immobilized in Accurel MP 1000. Response surface methodology was used for modeling and optimization of the reaction conditions catalyzed by immobilized YLL2. Central composite rotatable designs were performed as a function of the reaction time (2.5–49.5 h) and the molar ratio of medium chain fatty acid/TAG (MR; 0.6–7.4), for both acids, and also of temperature (32–48 ̊C) for C8:0 experiments. As for capric acid, the incorporation of caprylic acid in olive oil showed not to depend of the temperature, within the tested range. The response surfaces, fitted to the experimental data, were described by a first-order polynomial equation, for C8:0 incorporation, and by a second-order polynomial equation for C10:0 incorporation. Under optimized conditions (48 h reaction at 40 ̊C, with a molar ratio of 2:1 M/TAG) the highest incorporation was reached for C8:0 (25.6 mol%) and C10:0 (21.3 mol%).     

Synthesis of structured lipid with balanced omega-3: Omega-6 ratio by lipase-catalyzed acidolysis reaction: Optimization of reaction using response surface methodology

The present study deals with the production of structured lipid containing omega-3 and omega-6 fatty acids in the ratio of 1:1 by incorporating omega-3 fatty acids (α-linolenic acid) from linseed oil into groundnut oil using lipase (Lipozyme IM from Rhizomucor miehei) catalyzed acidolysis reaction in hexane. The reaction conditions were optimized by response surface methodology with a four-variable five-level central composite rotatable experimental design. The influence of four independent parameters, namely ratio of fatty acid concentrate from linseed to groundnut oil (0.66–1.98, w/w), reaction temperature (30–60 °C), enzyme concentration (1–5%) and reaction time (2–54 h) on omega-3 fatty acids incorporation into groundnut oil were optimized. Optimal conditions for the structured lipid containing omega-3 to omega-6 fatty acids in the ratio of 1:1 were determined to be; enzyme concentration 3.75% (w/w), temperature 37.5 °C, incubation time 30.81 h and ratio of free fatty acid concentrate from linseed oil to groundnut oil 1.16 (w/w).     

Reciprocal inhibition of in vitro substrate movement into avian skeletal muscle

Plasma glucose and ketone concentrations are much higher in birds than in humans and birds exhibit resistance to insulin-mediated glucose uptake into muscle. Therefore, birds may offer a model in which to examine the effects of high plasma glucose and free fatty acid (FFA) concentrations on substrate preference. The present study examined the uptake of radiolabeled oleic acid (OA; C18:1) and radiolabeled glucose by skeletal muscle isolated from the forewing of English sparrows (Passer domesticus). In dose–response studies, unlabeled glucose and OA (20 mM each) inhibited the uptake of their respective radiolabeled counterparts. To examine the effects of glucose on OA uptake, muscles were incubated for 60 min in a buffer containing 20 mM glucose with the addition of radiolabeled OA. This level of glucose significantly decreased radiolabeled OA uptake by 36%. Using the same methodology, 20 mM OA significantly decreased radiolabeled glucose transport by 49%. Comparing control values for glucose (0.952 ± 0.04 μM/mg muscle) and OA uptake (2.20 ± 0.29 μM/mg muscle), it is evident that OA is preferentially taken up by avian skeletal muscle. As FFAs provide a greater amount of energy per mole (146 ATP/OA) than carbohydrates (36 ATP/glucose), storing and utilizing fats may be more energy-efficient for birds. As studies in mammals have shown that FFAs may impair glucose uptake pathways, it is suspected that high FFA uptake by avian skeletal muscle may induce their notably lower glucose transport.     

Exploring a new,soluble lipase for FAMEs production in water-containing systems using crude soybean oil as a feedstock

Performance of a new lipase from Novozymes (Callera Trans L) was studied for fatty acid methylesters (FAMEs) production. In order to reduce the costs of the industrial enzymatic biodiesel production process, the enzyme was used in its soluble form instead of the common immobilized preparations. Cost reduction was also achieved by using crude (non-degummed) soybean oil as a cheaper raw material. The effect of water content during Callera Trans L-catalyzed FAMEs production was explored from evaluation of free fatty acids (FFAs), tri- di or monoacylglycerides (TAGs, DAGs, MAGs) variation during 24 h reaction. An excellent 96% FAMEs release was achieved when low (3–5%) water concentrations were used in the conversion of crude soybean oil. Time course HPLC analysis of the reaction products suggests that the soluble enzyme proceeds through a mechanism of methylester formation based on a first hydrolysis step that releases FFAs, DAGs or MAGs, followed by esterification of FFAs with methanol for FAMEs production.     

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.     

Determination of chloramphenicol,thiamphenicol, florfenicol,and florfenicol amine in poultry and porcine muscle and liver by gas chromatography-negative chemical ionization mass spectrometry

A sensitive and reliable method using gas chromatography-negative chemical ionization mass spectrometry (GC-NCI/MS) was developed for the simultaneous determination of chloramphenicol (CAP), thiamphenicol (TAP), florfenicol (FF), and florfenicol amine (FFA) at trace levels in muscle and liver. Before extraction with ethyl acetate, CAP-d₅ was added to tissue samples as internal standard. The organic extracts were frozen to remove lipid and further purified by liquid–liquid extraction (LLE) with hexane and solid-phase extraction (SPE) using Oasis HLB cartridges. The target compounds were derivatized with BSTFA + 1% TMCS prior to GC-NCI/MS determination in selected ion monitoring mode (SIM). The recovery values ranged from 78.5 to 105.5%, with relative standard deviations (RSD) <17%. The limits of detections (LODs) of 0.1 μg/kg for CAP and 0.5 μg/kg for TAP, FF, and FFA were obtain. Incurred sample and samples from local market were successfully analyzed using this method.     

Optimization of enzymatic hydrolysis of triglycerides in soy deodorized distillate with supercritical carbon dioxide

Enzymatic hydrolysis of triglycerides of soy deodorized distillate (DOD), using immobilized Candida rugosa lipase under supercritical carbon dioxide (SC-CO₂) medium, was carried out. Optimization of the reaction parameters using response surface methodology based on Box-Behnken model at three levels of pressure (120–180 bar), temperature (40–60 °C) and moisture content (40–80% of triglyceride content) for maximum hydrolysis of triglycerides was arrived by multilinear regression of the experimental results. The optimum conditions for maximum degree of triglyceride hydrolysis (94%) were found to be: pressure of 180 bar, temperature of 43 °C and moisture content of 40% to the triglyceride content. Maximum degree of hydrolysis was achieved with short incubation time of 1.5 h under SC-CO₂. Whereas conventional method of hydrolysis in hexane under similar reaction conditions of temperature, moisture and enzyme concentration, needs 5 h to achieve 88% of triglyceride hydrolysis.     

Passive heat loading links lipolysis and regulation of fibroblast growth factor-21 in humans

There is relativley little information on the serum biomarkers of heat stress. Therefore, the goal of this study was to verify the effect of passive heat loading (PHL) on the expression of fibroblast growth factor-21 (FGF21) and free fatty acids (FFAs). Four PHL protocols based on intensity (39 °C vs. 43 °C, leg immersion, 30 min) and type (leg vs. half immersion, 42 °C, 30 min) were used. Each protocol was applied on a 2 day cycle to 12 healthy adult males (age, 22.4±2.9 years; height, 174.1±4.6 cm; weight, 71.3±5.6 kg; body mass index, 23.1±3.0). The subjects were categorized into two groups according to the study design (randomized, with a parallel trial). Body temperature, FGF21 and FFAs were determined prior to PHL, immediately and 60 min after PHL. Body temperature was significant higher (43 °C) than the 39 °C measured under identical PHL type (leg immersion). PHL was effective for the expression of FGF21 and for lipolysis. The quantitative levels of FGF21 and FFA increased with increasing temperature (39 °C<42 °C<43 °C). A significant difference in the quantitative levels of FGF21 and FFAs was also evident based on the type of PHL (leg<half immersion) even when PHL was applied at the same temperature (42 °C). In conclusion, PHL was effective for expressing FGF21 and for lipolysis. Therefore, PHL may be expected to help in the reduction of body fat. Additionally, when the identical type (leg immersion) of PHL is applied, a loading temperature of 43 °C is more effective for expressing FGF21 and for lipolysis than temperatures of 39 °C and 42 °C, and half immersion is more effective than leg immersion at 42 °C.     

Kinetic study on enzymatic esterification of tuna fish oil fatty acids with butanol

Docosahexaenoic acid (DHA) is an important polyunsatured fatty acid (PUFA) which can be purified from tuna fish oil fatty acids by selective enzymatic esterification. The present paper investigates the kinetic study for selective esterification of tuna fish oil fatty acids with butanol catalyzed by Rhizopus oryzae lipase (ROL) in biphasic solvent system. Under the most suitable reaction conditions, 76.2% esterification was achieved in 24 h. Different kinetic models for esterification given by Segel [1], Oliveira et al. [2], Gogoi et al. [3], and Kraai et al. [4] were tested for fitting the esterification data and the model given by Oliveira et al. [2] was found to be most suitable. The model given by Prazeres et al. [5] for hydrolysis was also tested for esterification and the model with second order product inhibition was found to provide better match between the predicted and experimental values than that of model by Oliveira et al. [2]. The kinetic model was fitted using MATLAB^® to determine the best kinetic parameters. The average value of kinetic constants using the model given by Prazeres et al. were estimated as K_m = 23.6 μmoles FFA/ml, K_i1 = 4.6 × 10⁻⁵ μmoles FFA/mg enzyme h, K_i2 = 0.0062 μmoles FFA/mg enzyme h and K₂ = 149.5 μmoles FFA/mg enzyme h.     

FTIR determination of free fatty acids in fish oils intended for biodiesel production

Biodiesel is commonly derived from vegetable oils and animal (fish and livestock) fats by alkali- or lipase-catalyzed transesterification reactions. Since free fatty acid (FFA) content is a critical parameter in the conversion of fish oils to methyl esters, the performance of a Fourier transform infrared (FTIR) spectroscopic method was assessed as an alternative to the conventional AOCS titrimetric method. The FTIR method involves the simultaneous extraction of FFAs and their stoichiometric conversion to their salts using a weak base, sodium hydrogen cyanamide (NaHNCN) dissolved in methanol, followed by measurement of the carboxylate band, ν(COO^?), at 1573 cm^?1 relative to a baseline at 1820 cm^?1 in the differential spectrum of the methanol extract. With minor modifications, this method was found to be capable of responding linearly to oleic acid (0–6.5%) addition, producing a FFA calibration equation having a S.D. of ±0.014% FFA. FTIR and titrimetric analytical results were compared for samples prepared by standard addition as well as for fish oils extracted from salmon skin which had been stored up to 120 days at ?20 °C. Both methods responded in a comparable manner; however, the FTIR method was more reproducible and accurate as well as simpler to carry out and was deemed to be a better primary method than the titrimetric method. The FFA content of Atlantic salmon (Salmo salar) skin lipids increased linearly from ～0.6% to 4.5% within 120 days, likely as a result of autoxidation. It was concluded that the NaHNCN-based FTIR method is a flexible, viable instrumental alternative to the AOCS titrimetric procedure for the determination of FFA content of fish tissue lipids destined for biodiesel production.     

High hydrostatic pressure increased stability and activity of immobilized lipase in hexane

Lipases are important to high value product synthesis, modification, and enhancement. However, they are often unstable above 40 °C. While most current applications of high hydrostatic pressure (HHP) are for inactivating deleterious enzymes, there is evidence that HHP can stabilize and increase activity of some enzymes. This study examines the apparent kinetics of immobilized lipase-catalyzed synthesis of isoamyl acetate at HHP in hexane. HHP reduced thermal inactivation of lipase by up to 152% after 4 h at 80 °C and 400 MPa when compared to incubations at low pressure. No significant differences were found in activation energy (E_a) at different pressures, irrespectively of the pressurization and heating sequence, and were between 35.7 ± 3.5 and 47.8 ± 8.2 kJ mol^?1, depending on the method. In all methods utilized, activity at 63.5 and 80 °C at 400 MPa was greater (from about 20 to 96% increase) than at low pressure. Activity increased by 110% at low pressure versus a 239% increase at 350 MPa when the temperature was increased from 40 to 80 °C. Increasing pressure up to 350 MPa increased lipase activity while pressures greater than 350 MPa maintained or decreased lipase activity. Activation volume (ΔV^≠) appeared negative between ambient pressure and 200 MPa in contrast to a positive ΔV^≠ between 300 and 600 MPa. Apparent ΔV^≠ was 14.3 ± 1.7 or 15.2 ± 2.2 cm³ mol^?1 at 40 or 80 °C, respectively, between 300 and 500 MPa.     

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.     

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.     

Obesity,physical activity and cancer risks: Results from the Cancer,Lifestyle and Evaluation of Risk Study (CLEAR)

IntroductionPhysical activity (PA) has been associated with lower risk of cardiovascular diseases, but the evidence linking PA with lower cancer risk is inconclusive. We examined the independent and interactive effects of PA and obesity using body mass index (BMI) as a proxy for obesity, on the risk of developing prostate (PC), postmenopausal breast (BC), colorectal (CRC), ovarian (OC) and uterine (UC) cancers.MethodsWe estimated odds ratios (OR) and 95% confidence intervals (CI), adjusting for cancer specific confounders, in 6831 self-reported cancer cases and 1992 self-reported cancer-free controls from the Cancer Lifestyle and Evaluation of Risk Study, using unconditional logistic regression.ResultsFor women, BMI was positively associated with UC risk; specifically, obese women (BMI ≥30 kg/m²) had nearly twice the risk of developing UC compared to women with healthy-BMI-range (<25 kg/m²) (OR = 1.99;CI:1.31–3.03). For men, BMI was also positively associated with the risk of developing any cancer type, CRC and PC. In particular, obese men had 37% (OR = 1.37;CI:1.11–1.70), 113% (OR = 2.13;CI:1.55–2.91) and 51% (OR = 1.51;CI:1.17-1.94) higher risks of developing any cancer, CRC and PC respectively, when compared to men with healthy-BMI-range (BMI<25 kg/m²).Among women, PA was inversely associated with the risks of CRC, UC and BC. In particular, the highest level of PA (versus nil activity) was associated with reduced risks of CRC (OR = 0.60;CI:0.44–0.84) and UC (OR = 0.47;CI:0.27–0.80). Reduced risks of BC were associated with low (OR = 0.66;CI:0.51–0.86) and moderate (OR = 0.72;CI:0.57–0.91) levels of PA. There was no association between PA levels and cancer risks for men.We found no evidence of an interaction between BMI and PA in the CLEAR study.ConclusionThese findings suggest that PA and obesity are independent cancer risk factors.     

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.     

An organic solvent and thermally stable lipase from Burkholderia ambifaria YCJ01: Purification,characteristics and application for chiral resolution of mandelic acid

A solvent-tolerant bacterium Burkholderia ambifaria YCJ01 was newly isolated by DMSO enrichment of the medium. The lipase from the strain YCJ01 was purified to homogeneity with apparent molecular mass of 34 kDa determined by SDS-PAGE. The purified lipase exhibited maximal activity at a temperature of 60 °C and a pH of 7.5. The lipase was very stable below 55 °C for 7 days (remaining 80.3% initial activity) or at 30 °C for 60 days. PMSF significantly inhibited the lipase activity, while EDTA had no effect on the activity. Strikingly, the lipase showed distinct super-stability to the most tested hydrophilic and hydrophobic solvents (25%, v/v) for 60 days, and different optimal pH in contrast with the alkaline lipase from B. cepacia S31. The lipase demonstrated excellent enantioselective transesterification toward the S-isomer of mandelic acid with a theoretical conversion yield of 50%, ee_p of 99.9% and ee_s of 99.9%, which made it an exploitable biocatalyst for organic synthesis and pharmaceutical industries.     

Pancreatic lipase inhibitory and antioxidative constituents from the aerial parts of Paeonia lactiflora Pall. (Ranunculaceae)

To date, there have been reports mostly about research results of the peony root in comparison to the aerial parts. According to our study, the aerial parts of P.lactiflora showed superior anti-oxidative and pancreatic lipase inhibitory activities than its root. Especially, the water extract and the ethyl acetate fraction of the ethanol extract exhibited potent pancreatic lipase inhibitory activity by 53.11 ± 1.22% and 46.16 ± 1.55% at the same dose of orlistat (62.5 ± 1.27%). The ethanol extract exhibited the best anti-oxidative activity with IC₅₀ of 17.08 ± 0.9 μg/mL, and the ethyl acetate fraction 19.75 ± 0.02 μg/mL, respectively, comparing to the positive control rutin (IC₅₀, 22.66 ± 0.29 μg/mL). From the anti-oxidative and pancreatic lipase inhibitory active fractions three new compounds, monplacphloroside (1), monplachydroxyquinoside (2) and herbacetin-7-O-β-d-sophoroside (3) were isolated along with 19 (4-22) known ones.Compounds, PGG (14), 1-O-methyl-2,3,4,6-tetra-O-galloyl-β-d-glucopyranose (17) and ethylgallate (9) were found to be the strongest antioxidants and pancreatic lipase inhibitors. Monoterpenes, albiflorin R₂ (19) and albiflorin (20) were determined for the first time as strong pancreatic lipase inhibitors. The presence of the esterified galloyl moiety, with its increasing numbers or the β-lactone cycle within the molecular structure plays an essential role for the enhancement of the pancreatic lipase enzyme inhibitory activity.