Lipase-catalyzed synthesis of phenolic lipids from fish liver oil and dihydrocaffeic acid

The enzymatic synthesis of phenolic lipids by lipase-catalyzed transesterification of dihydrocaffeic acid (DHCA) with fish liver oil was investigated in a selected organic solvent medium. These synthesized phenolic lipids have potential use as nutraceutical products. Using a molar ratio of 1:8 DHCA to fish liver oil in hexane:2-butanone mixtures of 75:25 and 85:15 (v/v), the lipase-catalyzed reaction resulted in maximum conversion of 55.8 and 65.4%, respectively. The maximum conversion of phenolic monoacylglycerols in hexane:2-butanone mixture of 75:25 and 85:15 (v/v) was 40.3 and 37.7%, respectively; using the same solvent mixtures, the conversions of the phenolic diacylglycerol were 15.8 and 36.8%, respectively. Hexane:2-butanone mixture of 75:25 (v/v) was, therefore, the best organic solvent mixture for the production of phenolic monoacylglycerols, while that of 85:15 (v/v) was best for the production of phenolic diacylglycerols. The phenolic lipids produced from the fish liver oil and DHCA demonstrated antioxidant property as indicated by its free radical scavenging capacity.     

Lipase-catalyzed synthesis of phenolic lipids from fish liver oil and dihydrocaffeic acid

The enzymatic synthesis of phenolic lipids by lipase-catalyzed transesterification of dihydrocaffeic acid (DHCA) with fish liver oil was investigated in a selected organic solvent medium. These synthesized phenolic lipids have potential use as nutraceutical products. Using a molar ratio of 1:8 DHCA to fish liver oil in hexane:2-butanone mixtures of 75:25 and 85:15 (v/v), the lipase-catalyzed reaction resulted in maximum conversion of 55.8 and 65.4%, respectively. The maximum conversion of phenolic monoacylglycerols in hexane:2-butanone mixture of 75:25 and 85:15 (v/v) was 40.3 and 37.7%, respectively; using the same solvent mixtures, the conversions of the phenolic diacylglycerol were 15.8 and 36.8%, respectively. Hexane:2-butanone mixture of 75:25 (v/v) was, therefore, the best organic solvent mixture for the production of phenolic monoacylglycerols, while that of 85:15 (v/v) was best for the production of phenolic diacylglycerols. The phenolic lipids produced from the fish liver oil and DHCA demonstrated antioxidant property as indicated by its free radical scavenging capacity.     

Temperature dependence of the structural dimensions of the inverted hexagonal (HII) phase of phosphatidylethanolamine-containing membranes

The characteristic temperature dependence of the lattice basis vector length d of phospholipid-water systems in the inverted hexagonal (HII) phase has been investigated with X-ray diffraction. For 1,2-dioleoyl-sn-glycero-3-phosphoethanolamine (DOPE), d falls sharply from 78.1 A at 10 degrees C to 62.5 A at 90 degrees C. When used in conjunction with the volume fractions of the constituents, d can be used to determine the dimensions within the lipid and water regions. These data showed that a reduction in the radius of the HII-phase water cylinders Rw accounted for most of the reduction in d. From geometrical relationships between the dimensions in the HII phase, it was shown that both d and Rw are sensitive functions of the thickness of the lipid monolayer dHII. The characteristic shape of d(T) could be parameterized with the small temperature dependence of dHII along with the ratio v/a, which is the ratio of the specific volume to the area per lipid molecule at the polar interface. The ratio v/a was found to be independent of temperature for the fully hydrated HII system. Additional measurements made with a mixture of DOPE and 1,2-dioleoyl-sn-glycero-3-phosphocholine (DOPC), mole ratio 5.07:1, produced a similar parameterization of d(T). The larger basis vector lengths for this mixture compared to those for DOPE can be attributed to a smaller ratio of v/a, which was also found to be temperature independent for this mixture. The smaller value of v/a is due to the larger effective headgroup area of DOPC.(ABSTRACT TRUNCATED AT 250 WORDS)     

Sex attractants for six moth species of the families Brachodidae, Choreutidae and Tineidae from Kazakhstan and Lithuania

Sex attractants were established for one Brachodidae, three Choreutidae and two Tineidae moth species during field screening tests with (2E,13Z)-octadecadien-1-al, (2E,13Z)-, (3E,13Z)-, (3Z,13Z)-octadecadien-1-ols and their acetates (2E,13Z-18:Ald, 2E,13Z-, 3E,13Z-, 3Z,13Z-18:OH/OAc) as well as of binary mixtures of these compounds in West-Kazakhstan and Lithuania. Males of Brachodes appendiculata were attracted by 3E,13Z-18:OAc, Prochoreutis ultimana and P. myllerana by 2E,13Z-18:OH, Monopis palidella by 2E,13Z-18:Ald and Triaxomera fulvimitrella by binary mixtures of 3Z,13Z-18:OAc with either 3E,13Z-18:OH in the ratio of 5:5 or 3Z,13Z-18:OH in the ratio of 9:1 (v/v). The 3-component mixture composed of 2E,13Z-18:OH, 3Z,13Z-18:OH and 2E,13Z-18:Ald in the ratio 1:1:1 was developed to attract Prochoreutis sehestediana males. Attraction antagonists for B. appendiculata, P. ultimana and M. palidella were shown.     

Development of an acetone/water fractional precipitation process for purification of paclitaxel from plant cell cultures

This study investigated the efficiency of acetone/water fractional precipitation for the purification of paclitaxel from plant cell cultures. Adding distilled water at room temperature into an acetone solution of dissolved crude extract until the acetone/water ratio became 40:60, 30:70, 20:80, and 10:90 (v/v) and stirring the mixture for 10 min at room temperature resulted in paclitaxel yields of 54.3, 89.1, 95.5, and 97.6%, respectively. With an acetone/water ratio of 40:60, v/v, a high yield of paclitaxel (84.8 ~ 86.0%) was produced by an additional 2 h storage at a low temperature (4oC) without additional mixing, or at room temperature with additional mixing. In contrast, preparing the 40:60 (v/v) acetone/water mixture at a low temperature (4oC) and mixing for 10 min at a low temperature, a similar high yield (~ 87.9%) of paclitaxel was obtained immediately. Thus, increasing the proportion of distilled water, or decreasing the temperature of the added water were confirmed as important for obtaining high yields of paclitaxel by acetone/water fractional precipitation.     

Lipase-catalyzed acidolysis of fish liver oil with dihydroxyphenylacetic acid in organic solvent media

Lipase-catalyzed acidolysis reaction of fish liver oil with dihydroxyphenylacetic acid (DHPA) was investigated in terms of enzyme specificity as well as the effects of enzyme concentration, molar substrate ratio and organic solvent mixture on the bioconversion yield. The highest bioconversion yield of 83% was obtained when Novozym 435 was used as biocatalyst in a hexane:2-butanone mixture of 75:25 (v/v) at a fish liver oil to DHPA substrate molar ratio of 4:1; however, lower bioconversion yield (15%) was obtained when Lipozyme IM 20 was used. The bioconversion yield of phenolic monoacylglycerols (MAGs) increased from 11 to 70% when the ratio of the hexane/2-butanone reaction medium was changed from 85:15 to 75:25 (v/v), whereas that of phenolic diacylglycerols (DAGs) remained relatively unchanged (13–16%). The results also showed that the acidolysis reaction resulted in an increase of C_20:5 ω-3 and C_22:6 ω-3 proportions from 11.5 and 20.2% in the original fish liver oil to 22.6–27.1 and 22.8–23.1% in the phenolic lipids, respectively. The radical scavenging ability of phenolic lipids was determined to be about half-time lower than that of α-tocopherol.     

Enzymatic esterification of dihydrocaffeic acid with linoleyl alcohol in organic solvent media

The enzymatic esterification of dihydrocaffeic acid with linoleyl alcohol, using immobilized lipases (Lipozyme IM 20 and Novozym 435), was investigated in selected organic solvent media. Novozym 435 was found to be more efficient for catalyzing the esterification reaction. The highest enzymatic activity of 0.89 μmol esterified linoleyl alcohol/g solid enzyme/min was obtained in a hexane/2-butanone mixture of 75:25 (v/v), with an esterification yield of 75%; however, an increase in the 2-butanone proportion in the mixture up to 50% (v/v) resulted in a decrease in enzymatic activity and esterification yield to 0.38 μmol esterified linoleyl alcohol/g solid enzyme/min and 40%, respectively. The maximum esterification yield of 99.3% was obtained with a dihydrocaffeic acid to linoleyl alcohol ratio of 1:8. The electrospray ionization-mass spectroscopic structural analysis of the end products confirmed the biosynthesis of dihydrocaffeic acid ester of linoleyl alcohol, which demonstrated an anti-radical activity using 2,2-diphenyl-1-picrylhydrazyl as a radical model.     

Potential availability of anaerobic treatment with digester slurry of animal waste for the reclamation of acid mine water containing sulfate and heavy metals

The use of an anaerobic digester slurry of cattle waste for the reclamation of acid mine water was examined. When the digester slurry was mixed with acid mine water, anaerobic digestion, including sulfate reduction and methanogenesis, was enhanced. In the mixture of acid mine water and the digester slurry, sulfate reduction proceeded without diminishing methanogenesis. The digester slurry and its supernatant (SDF-sup) showed a significant capacity to act as a strong alkaline reagent, and the pH of the acid mine water was markedly elevated by the addition of the digester slurry of SDF-sup even at the low ratio of 1% (v/v). Precipitation of heavy metals in the acid mine water occurred as the pH was elevated by the addition of SDF-sup. When the digester slurry was added at the ratio of 5% (v/v) to acid mine water which had been pretreated with SDF-sup, the rate of sulfate reduction increased with increasing the concentration of sulfate in the mixture up to about 1,400 mg·l⁻¹. In acid mine water pretreated with SDF-sup and supplemented with the digester slurry at the ratio of 5% (v/v), the maximum amount of sulfate reduced within 20 d of incubation was about 1,000 mg·l⁻¹, and the maximum rate of sulfate reduction was about 120 mg SO₄²⁻·l⁻¹·d⁻¹.     

Lipase-catalyzed synthesis of monoacylglycerol in a homogeneous system

The 1,3-regiospecifique lipase, Lipozyme IM, catalyzed the esterification of lauric acid and glycerol in a homogeneous system. To overcome the drawback of the insolubility of glycerol in hexane, which is extensively used in enzymatic synthesis, a mixture of n-hexane/tert-butanol (1:1, v/v) was used leading to a monophasic system. The conversion of lauric acid into monolaurin was 65% in 8 h, when a molar ratio of glycerol to fatty acid (5:1) was used with the fatty acid at 0.1 M, and the phenomenon of acyl migration was minimized.     

Enzymatic in situ saccharification of cellulose in aqueous-ionic liquid media

The enzymatic saccharification of a model cellulosic substrate, Avicel PH-101, using an ionic liquid (IL), 1-ethyl-3-methylimidazolium diethylphosphate, was explored. After mixing the IL solution of cellulose with different volumes of 10 mM citrate buffer (pH 5.0), cellulase was directly added to the aqueous-IL mixture at 40°C. When the volume of IL to water was greater than 3:2, little cellulase activity was observed. However, decreasing the volume ratio markedly enhanced enzymatic activity: an IL to water ratio of 1:4 (v/v) resulted in over 70% of the starting amount of cellulose (10 mg/ml) being converted to glucose and cellobiose.     

Growth of Candida utilis on ethanol and isopropanol

Candida utilis grew on ehtanol and an ethanol-isopropanol-water (22:2:1 vols) mixture but not on isopropanol alone. Acetone accumulated in all cultures containing isopropranol but its presence in the alcohol mixture did not lower growth rate or yield significantly when compared with growth experiments on ethanol alone. Growth rate and yield declined at ethanol concentrations greater than 1% (v/v) and 0.3% (v/v) respectively. In a 0.3% (v/v) alcohol mixture, acetate was found only during the exponential growth phase. In a 3% (v/v) mixture, acetate and ethyl acetate accumulated during growth whereas acetaldehyde was present only during the exponential growth phase.     

Co-fermentation of grape must by Issatchenkia orientalis and Saccharomyces cerevisiae reduces the malic acid content in wine

Grape must was fermented by a mixed culture of Saccharomyces cerevisiae W-3 (a wine yeast) and Issatchenkia orientalis KMBL 5774 (a malic acid-degrading yeast). Co-fermentation with 1:1 (v/v) inoculum ratio of W-3 and KMBL 5774 decreased malic acid to 0.33 mg/ml from 1.1 mg ml with W-3 alone. Ethanol production was the same in both cases (7.8%, v/v). Acetaldehyde, 1-propanol, 2-butanol and isoamyl alcohol all decreased, with an increase in methanol, in the co-fermented wine. Sensory evaluation showed a higher score in the wine fermented with 1:1 (v/v) inoculum ratio than those obtained by 4:1 (v/v) inoculum ratio or W-3 alone.     

Comparing submerged and solid-state fermentation of agro-industrial residues for the production and characterization of lipase by Trichoderma harzianum

Lipase production by Trichoderma harzianum was evaluated in submerged fermentation (SF) and solid-state fermentation (SSF) using a variety of agro-industrial residues. Cultures in SF showed the highest activity (1.4 U/mL) in medium containing 0.5 % (w/v) yeast extract, 1 % (v/v) olive oil and 2.5 C:N ratio. This paper is the first to report lipase production by T. harzianum in SSF. A 1:2 mixture of castor oil cake and sugarcane bagasse supplemented with 1 % (v/w) olive oil showed the best results among the cultures in SSF (4 U/g ds). Lipolytic activity was stable in a slightly acidic to neutral pH, maintaining 50 % activity after 30 min at 50 °C. Eighty percent of the activity remained after 1 h in 25 % (v/v) methanol, ethanol, isopropanol or acetone. Activity was observed with vegetable oils (olive, soybean, corn and sunflower) and long-chain triacylglycerols (triolein), confirming the presence of a true lipase. The results of this study are promising because they demonstrate an enzyme with interesting properties for application in catalysis produced by fermentation at low cost.     

Comparison of performance of C18 monolithic rod columns and conventional C18 particle-packed columns in liquid chromatographic determination of Estrogel and Ketoprofen gel

The performance of monolithic HPLC columns Chromolith (made by Merck, Germany) and conventional C18 columns Discovery (Supelco, Sigma-Aldrich, Prague, Czech Republic) was tested and the comparison for two topical preparations Ketoprofen gel and Estrogel gel was made. The composition of mobile phases - for Ketoprofen analysis a mixture of acetonitrile, water and phosphate buffer adjusted to pH 3.5 (40:58:2) and for Estrogel analysis a mixture of acetonitrile, methanol, water (23:24:53) - was usually not optimal for analyses at all types of columns. Thus an adjustment of components ratio was necessary for sufficient resolution of the compounds analysed. Various flow rates (1.0-5.0 ml/min) and mobile phases (usually increasing ratio of water content) were applied. Determination of active substances, preservatives and impurities and comparison of retention times and system suitability test parameters was accomplished. For Estrogel gel, following chromatographic conditions were found: using Chromolith Flash RP-18e monolith column, mobile phase was acetonitrile, methanol, water (13:24:63, v/v/v) and flow-rate 3.0 ml/min. Using monolith column ChromolithSpeedROD RP-18e, the mobile phase was acetonitrile, methanol, water (18:24:58, v/v/v) and flow-rate 4.0 ml/min. For the monolith column Chromolith Performance RP-18e, the mobile phase was acetonitrile, methanol, water (23:24:53, v/v/v), flow-rate 3.0ml/min. Analysis of Ketoprofen gel gave the best results using following analytical conditions: for monolith column Chromolith Flash RP-18e, mobile phase as a mixture of acetonitrile, water, phosphate buffer pH 3.5 (30:68:2, v/v/v) was used, at flow-rate 2.0 ml/min. For ChromolithSpeedROD RP-18e monolith column, acetonitrile, water, phosphate buffer pH 3.5 (35:63:2, v/v/v) was used as a mobile phase at flow-rate 3.0 ml/min. Chromolith Performance RP-18e gave the best results using mobile phase acetonitrile, water, phosphate buffer pH 3.5 (30:68:2, v/v/v) at the flow-rate 5.0 ml/min. It was proved that monolith columns, due to their porosity and low back-pressure, can save analysis time by about a factor of three with sufficient separation efficiency. Thus, for example 11 min long analysis can be performed in 4 min with comparable results.     

Fast, efficient reconstitution of the cyclooxygenases into proteoliposomes

To study the physical and catalytic properties of purified membrane proteins, it is often necessary to reconstitute them into lipid bilayers. Here, we describe a fast efficient method for the direct incorporation of cyclooxygenase-1 and -2 (COX-1 and -2) isozymes into liposomes without loss of activity. Purified COX-1 and -2 spontaneously incorporate into large unilamellar vesicles produced from a mixture of DOPC:DOPS (7:3) that has been doped with oleic acid. When incorporation was measured by comparing cyclooxygenase activity to total phospholipid in the proteoliposomes, molar reconstitution ratios of 1000:1 (phospholipid:COX) were obtained. Electron paramagnetic resonance spectroscopic spin counting analysis of proteoliposomes formed with nitroxide spin-labeled COX-2 gave a nearly identical phospholipid:COX ratio, confirming that incorporation had no effect on enzyme activity, and demonstrating that the efficiency of protein incorporation is sufficient for EPR spectroscopic analysis. The spontaneous incorporation of cyclooxygenase into intact liposomes allows only insertion into the outer leaflet for this monotopic enzyme, an orientation confirmed by immunogold staining of the proteoliposomes. This method of reconstitution into liposomes may be generally applicable to the class of monotopic integral membrane proteins typified by the cyclooxygenase isozymes.     

Early stages in the trifluoroethanol-induced unfolding of hen egg-white lysozyme and its complex with (GlcNAc)3

The trifluoroethanol-induced unfolding of hen egg-white lysozyme was studied by circular dichroism. It was shown that if the H2O/trifluoroethanol ratio is above 10:1 (v/v), the unique three-dimensional structure of the protein is not affected, whereas within the ration 10:1-2.8:1 (v/v), this structure is partially unfolded. At the ratio 2.4:1 (v/v), the native conformation of lysozyme is completely disrupted and the conformational transition fits a two-state model. A similar effect was observed for the trifluoroethanol-induced unfolding of the lysozyme-(GlcNAc)3 complex. Within the H2O2 trifluoroethanol ratio 15:1-5.5:1 (v/v), the characteristic intensities of the Cotton effects which arise from the association of (GlcNAc)3 with the active site of lysozyme, diminished and approached those exhibited by lysozyme itself at the same H2O trifluoroethanol ratios. This shows that (GlcNAc)3 is released from the protein surface in early stages of the unfolding process. At the ratio 2.4:1 (v/v), the lysozyme-(GlcNAc)3 complex was completely disrupted and the protein unfolded. It is suggested that a considerable alteration in hydration of the lysozyme molecule caused by trifluoroethanol increases protein surface fluctuations, causing the release of (GlcNAc)3 from the active site of lysozyme.     

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.     

Structural study of phosphomannan-protein complex of Citeromyces matritensis containing beta-1,2 linkage. Application of partial acid degradation and acetolysis techniques under mild conditions

The phosphomannan-protein complex of Citeromyces matritensis IFO 0651 strain was investigated for its chemical structure by a sequential degradation procedure, partial acid degradation followed by acetolysis under mild conditions. Upon treatment with 10 mM HCl at 100 degrees C for 1 h, this complex released mannotriose and mannotetraose consisting solely of 1,2-linked beta-D-mannopyranosyl residues, ca. 20% on weight basis of the parent complex. The acid-degraded complex was then subjected to acetolysis using an acetolysis medium of low sulfuric acid concentration, a 100:100:1 (v/v) mixture of acetic anhydride, acetic acid, and sulfuric acid at 40 degrees C for 36 h. A phosphate-containing manno-oligosaccharide fraction eluted in the void-volume region of a Bio-Gel P-2 column was found to consist of Manp beta 1----2Manp beta 1----2Manp alpha 1----2Man to which 1 mol of phosphate group was attached, while a manno-oligosaccharide fraction eluted in the diffusable region was a mixture of Manp beta 1----2Manp beta 1----2Manp beta 1----2Manp alpha 1----2Man, Manp beta 1----2Manp beta 1----2Manp alpha 1----2Man, Manp beta 1----2Manp alpha 1----2Man, Manp alpha 1----2Man, and mannose in the molar ratio of 0.08:0.33:0.19:0.32:1.00. Therefore, the structural analysis of the polysaccharide moiety of a beta-1,2 linkage-containing phosphomannan-protein complex of fungal origin can be achieved by means of a sequential degradation procedure, partial acid degradation followed by acetolysis under mild conditions.     

Isolation of γ-aminobutyric acid-producing bacteria and optimization of fermentative medium

Ten γ-aminobutyric acid (GABA)-producing lactic acid bacteria (LAB) strains were isolated from kimchi and yoghurt. The strain B, isolated from kimchi showed the highest GABA-producing ability (3.68 g/L) in MRS broth with 1% monosodium glutamate (MSG). Strain B was identified as Lactococcus lactis subsp. lactis. The GABA-producing ability of L. lactis B was investigated using brown rice juice, germinated soybean juice and enzymolyzed skim milk as medium compositions. The D-optimal mixture design was applied to optimize the ratio of the three kinds of components in the media. The results showed that when the mixing ratio of brown rice juice, germinated soybean juice and enzymolyzed skim milk was 33:58:9 (v:v:v), the maximum GABA yield of L. lactis B was 6.41 g/L.     

Analysis of Oxcarbazepine and the 10‐Hydroxycarbazepine Enantiomers in Plasma by LC‐MS/MS: Application in a Pharmacokinetic Study

Oxcarbazepine is a second‐generation antiepileptic drug indicated as monotherapy or adjunctive therapy in the treatment of partial seizures or generalized tonic–clonic seizures in adults and children. It undergoes rapid presystemic reduction with formation of the active metabolite 10‐hydroxycarbazepine (MHD), which has a chiral center at position 10, with the enantiomers (S)‐(+)‐ and R‐(?)‐MHD showing similar antiepileptic effects. This study presents the development and validation of a method of sequential analysis of oxcarbazepine and MHD enantiomers in plasma using liquid chromatography with tandem mass spectrometry (LC‐MS/MS). Aliquots of 100 μL of plasma were extracted with a mixture of methyl tert‐butyl ether: dichloromethane (2:1). The separation of oxcarbazepine and the MHD enantiomers was obtained on a chiral phase Chiralcel OD‐H column, using a mixture of hexane:ethanol:isopropanol (80:15:5, v/v/v) as mobile phase at a flow rate of 1.3 mL/min with a split ratio of 1:5, and quantification was performed by LC‐MS/MS. The limit of quantification was 12.5 ng oxcarbazepine and 31.25 ng of each MHD enantiomer/mL of plasma. The method was applied in the study of kinetic disposition of oxcarbazepine and the MHD enantiomers in the steady state after oral administration of 300 mg/12 h oxcarbazepine in a healthy volunteer. The maximum plasma concentration of oxcarbazepine was 1.2 µg/mL at 0.75 h. The kinetic disposition of MHD is enantioselective, with a higher proportion of the S‐(+)‐MHD enantiomer compared to R‐(?)‐MHD and an AUC^0‐12 _{S‐(+)/R‐(?)} ratio of 5.44. Chirality 25:897–903, 2013. © 2013 Wiley Periodicals, Inc.