Screening of microbial esterases for asymmetric hydrolysis of 2-ethylhexyl butyrate

Summary A pH indicator agar plate method was used to screen for esterase activities for hydrolysis of 2-ethylhexyl butyrate. Seven hundred and fifty-seven selected microbial cultures, including 325 bacteria, and 432 yeasts and actinomycetes from the ARS Culture, Collection, were screened. Among them, 62 cultures hydrolyzed 2-ethylhexyl butyrate. Of these strains only 17 showed lipase activity on a rhodamine B lipase screen. The reaction products, 2-ethyl-1-hexanol andn-butyric acid were confirmed by gas-liquid chromatography (GC) and GC/MS analyses. The yield of 2-ethyl-1-hexanol varied depending on the strains of the microorganisms, with the highest yield at 79.1% by a strain ofPseudomonas myxogenes Product analyses with a cyclodextrin GC chiral column showed that two strains ofPseudomonas produced, greater than 80% enantiomeric excess of S(+)-2-ethyl-1-hexanol.     

Esterification of fatty acids using Candida antarctica lipase A in water-abundant systems

The feasibility of using native lipase A from Candida antarctica (CAL-A) to esterify fatty acids with water-insoluble alcohols in the presence of excess water was investigated in stirred-tank reactors. For high reaction rates, a ratio of water:substrates of 0.6-1.4:1 (v/v) was required. CAL-A showed higher substrate selectivity for the esterification of saturated palmitic acid with branched-chain 2-ethyl-1-hexanol than for unsaturated oleic acid with linear alcohol (1-decanol). After 18 h at 70 °C in a 1.5 l bulk stirred-tank reactor, an 2-ethyl-1-hexyl palmitic acid ester was obtained near 100 % yield [molar ratio palmitic acid:2-ethyl-1-hexanol ~1:1.25, with 1.11 % (w/w) Novocor ADL (based on palmitic acid weight)].     

Ionic liquids as a reaction medium for lipase-catalyzed methanolysis of sunflower oil

Ionic liquids, 1-butyl-3-methyl imidazolium hexafluorophosphate ([BMIm][PF₆]) and 1-ethyl-3-methyl imidazolium hexafluorophosphate ([EMIm][PF₆]), were used for the methanolysis of sunflower oil using Candida antarctica lipase (Novozyme 435) and gave yields of fatty acid methyl esters at 98–99% within 10 h. The optimum conditions of methanolysis in hydrophobic ionic liquids are 2% (w/w) lipase, 1:1 (w/w) oil/ionic liquid and 1:8 (mol/mol) oil/methanol at 58–60°C. Methanolysis using hydrophilic ionic liquids, 3-methyl imidazolium tetrafluoroborate ([HMIm][BF₄]) and 1-butyl-3-methyl imidazolium tetrafluoroborate ([BMIm][BF₄]), gave very poor yields. A hydrophobic ionic liquid thus protects the lipase from methanol. Recovered ionic liquids and lipase were used for four successive reaction cycles without any significant loss of activity.     

Lipase-catalysed synthesis of ester oils from biodiesel by-products

Ester oils obtained from natural long-chain fatty acids and alcohols are versatile substitutes for many petroleum-based products. Their efficient synthesis with the solvent-free esterification of free fatty acids (FFA) from by-products of biodiesel fabrication and 2-ethyl-1-hexanol with immobilised lipase from Thermomyces lanuginosa was investigated. The immobilisation of the biocatalyst in static emulsion yielded a specific esterification activity that was higher by a factor of 4.9–9.4 than the activity of the native enzyme. Favourable properties of the silicone-based immobilisation matrix in terms of stability and immobilisation yield were observed. In biodiesel by-products, the immobilised lipase catalysed the esterification of FFA as well as the transesterification of residual fatty acid methyl esters (FAME) to the desired ester oils. A conversion of 90% FFA and 35% FAME gave a total yield of 60%. The inactivation coefficients during repeated use in a stirred-tank reactor with intermittent pressure reduction were exceptionally low.     

Lipase-catalyzed resolution of primary alcohol containing quaternary chiral carbon

Summary 2-Cyano-2-phenyl-1-hexanol containing chiral quaternary carbon was resolved using a lipase. Among various reaction conditions, transesterification reaction (solvent; n-hexane, lipase; Candida cylindracea) gave high selectivity(20/80). Additionally, the selectivity could be improved(13/87) when pyridine(1%) was used as an additive. The ratios of resolved alcohols were determined by GC and ¹H-NMR analysis using Mosher's derivative.     

Production of trimethylolpropane esters of rapeseed oil fatty acids by immobilized lipase

The polyol, trimethylolpropane (2-ethyl-2-hydroxymethyl-1,3-propanediol), and a mixture of rapeseed oil fatty acid methyl esters were transesterified by immobilized lipases without additional organic solvent. The conversion to the polyol tri-ester with immobilized Rhizomucor mieheilipase Lipozyme IM 20 was about 75% after 24 h at 58°C, 5.3 kPa, with no added water, and the highest conversion of about 90% was reached in 66 h.     

Phase partition of gaseous hexane and surface hydrophobicity of Fusarium solani when grown in liquid and solid media with hexanol and hexane

The filamentous fungus, Fusarium solani, was grown in liquid and solid culture with glucose, glycerol, 1-hexanol and n-hexane. The partition coefficient with gaseous hexane (HPC) in the biomass was lower when grown in liquid medium with 1-hexanol (0.4) than with glycerol (0.8) or glucose (1) The HPC for surface growth were 0.2 for 1-hexanol, 0.5 for glycerol, 0.6 for glucose, and 0.2 for F. solani biomass obtained from a biofilter fed with gaseous n-hexane. These values show a 200-fold increase in n-hexane solubility when compared to water (HPC = 42). Lower HPC values can be partially explained by increased lipid accumulation with 1-hexanol, 10.5% (w/w) than with glycerol (8.5% w/w) or glucose (7.1% w/w). The diameter of the hyphae diminished from 3 μm to 2 μm when F. solani was grown on solid media with gaseous n-hexane thereby doubling the surface area for gaseous substrate exchange. The surface hydrophobicity of the mycelia increased consistently with more hydrophobic substrates and the contact angle of a drop of water on the mycelial mat was 113° when grown on n-hexane as compared to 75° with glucose. The fungus thus adapts to hydrophobic conditions and these changes may explain the higher uptake of gaseous hydrophobic substances by fungi in biofilters.     

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.     

Properties of a membrane-bound triglyceride lipase of rapeseed (Brassica napus L.) cotyledons

The properties of the alkaline lipase activity (EC 3.1.1.3) that was recovered almost completely from a microsomal membrane fraction of 4-d-old rapeseed (Brassica napus L.) cotyledons were studied employing a titrimetric test procedure. The apparent K_M was 6.5 mmol l^-1, with emulgated sunflower oil as the substrate. The products of triglyceride hydrolysis in vitro were glycerol, free fatty acids, and minor amounts of mono- and diglycerides. Maximum lipase activity depended on the preincubation of the lipolytic membrane fraction in 0.15 mol l^-1 NaCl and on the presence of at least 0.1 mol l^-1 NaCl in the test mixture. Desoxycholate and up to 0.1 mol l^-1 CaCl₂ also activated the enzyme while EDTA and detergents such as trito x-100, digitonin, tween 85, and sodium dodecylsulfate were inhibitory. The rapeseed lipase displayed a conspicuous substrate selectivity among different plant triglycerides; the activity was inversely correlated with the oleic acid content of the oils. Water-soluble triacetin and the phospholipid lecithin were not hydrolyzed. Increasing amounts of free fatty acids reduced lipase activity; erucic acid, a major component of rapeseed oil, exhibited the strongest effect, suggesting a possible role in the regulation of lipase activity in vivo. The data demonstrate that the lipolytic membrane fraction houses a triglyceride lipase with properties similar to other plant and animal lipases. It can both qualitatively and quantitatively account for the fat degradation in rapeseed cotyledons. The evidence that provides further reason to acknowledge the membranous appendices of the spherosomes as the intracellular site of lipolysis is discussed.     

Purification of lipase derived from Burkholderia pseudomallei with alcohol/salt-based aqueous two-phase systems

Alcohol/salt-based aqueous two-phase systems (ATPSs) were used to recover lipase derived from Burkholderia pseudomallei (B. pseudomallei). Nine biphasic systems, comprised of an alcohol-based top phase (ethanol, 2-propanol and 1-propanol) and a salt-based bottom phase (ammonium sulfate, potassium phosphate and sodium citrate), were evaluated for their effectiveness in lipase recovery. The stability of lipase in each of the solutions was tested, and phase diagrams were constructed for each system. The optimum partition efficiency for the purification of lipase was obtained in an ATPS of 16% (w/w) 2-propanol and 16% (w/w) phosphate in the presence of 4.5% (w/v) NaCl. The purified lipase had a purification factor of 13.5 and a yield of 99%.     

Lipase-catalysed synthesis of ester oils from biodiesel by-products

Ester oils obtained from natural long-chain fatty acids and alcohols are versatile substitutes for many petroleum-based products. Their efficient synthesis with the solvent-free esterification of free fatty acids (FFA) from by-products of biodiesel fabrication and 2-ethyl-1-hexanol with immobilised lipase from Thermomyces lanuginosa was investigated. The immobilisation of the biocatalyst in static emulsion yielded a specific esterification activity that was higher by a factor of 4.9-9.4 than the activity of the native enzyme. Favourable properties of the silicone-based immobilisation matrix in terms of stability and immobilisation yield were observed. In biodiesel by-products, the immobilised lipase catalysed the esterification of FFA as well as the transesterification of residual fatty acid methyl esters (FAME) to the desired ester oils. A conversion of 90% FFA and 35% FAME gave a total yield of 60%. The inactivation coefficients during repeated use in a stirred-tank reactor with intermittent pressure reduction were exceptionally low.     

Lipase production by Trichosporon fermentans WU-C12, a newly isolated yeast

From the soil samples of various locations, 245 strains of microorganisms were isolated by the enrichment culture method using olive oil as a carbon source. Of these microorganisms one deuteromycotinous yeast was the best producer of extracellular lipase, and the strain WU-C12 was identified as Trichosporon fermentans from the morphological and taxonomical properties. When cultivated at 30°C for 4 d in the medium containing 8% (w/v) corn steep and 3% (v/v) olive oil as sources of nitrogen and carbon, T. fermentans WU-C12 produced 126 U/ml of extracellular lipase. When 3% (v/v) tung oil was used instead of 3% (v/v) olive oil, 146 U/ml of the lipase was produced. Although lipase production decreased to 40 U/ml by the addition of 2% (w/v) glucose to the corn steep-olive oil medium, the strain WU-C12 produced 34 U/ml of lipase in the medium containing 2% (w/v) glucose instead of 3% (v/v) olive oil. On the other hand, T. fermentans WU-C12 could grow and produce lipase in the medium containing n-paraffin as a carbon source.     

Lipase-catalyzed biodiesel production from waste activated bleaching earth as raw material in a pilot plant

The production of fatty acid methyl esters (FAMEs) from waste activated bleaching earth (ABE) discarded by the crude oil refining industry using lipase from Candida cylindracea was investigated in a 50-L pilot plant. Diesel oil or kerosene was used as an organic solvent for the transesterification of triglycerides embedded in the waste ABE. When 1% (w/w) lipase was added to waste ABE, the FAME content reached 97% (w/w) after reaction for 12 h at 25 degrees C with an agitation rate of 30 rpm. The FAME production rate was strongly dependent upon the amount of enzyme added. Mixtures of FAME and diesel oil at ratios of 45:55 (BDF-45) and 35:65 (BDF-35) were assessed and compared with the European specifications for biodiesel as automotive diesel fuel, as defined by pr EN 14214. The biodiesel quality of BDF-45 met the EN 14214 standard. BDF-45 was used as generator fuel, and the exhaust emissions were compared with those of diesel oil. The CO and SO2 contents were reduced, but nitrogen oxide emission increased by 10%. This is the first report of a pilot plant study of lipase-catalyzed FAME production using waste ABE as a raw material. This result demonstrates a promising reutilization method for the production of FAME from industrial waste resources containing vegetable oils for use as a biodiesel fuel.     

The impact of reducing fatty acid desaturation on the composition and thermal stability of rapeseed oil

Oilseed rape (Brassica napus) is the third largest source of vegetable oil globally. In addition to food uses, there are industrial applications that exploit the ability of the species to accumulate the very‐long‐chain fatty acid (VLCFA) erucic acid in its seed oil, controlled by orthologues of FATTY ACID ELONGASE 1 (Bna.FAE1.A8 and Bna.FAE1.C3). The proportion of polyunsaturated fatty acids (PUFAs) in rapeseed oil is predicted to affect its thermal stability and is controlled by orthologues of FATTY ACID DESATURASE 2, particularly Bna.FAD2.C5. Our aim was to develop rapeseed lines combining high erucic and low PUFA characters and to assess the impact on thermal stability of the oil they produce. The new type of rapeseed oil (high erucic low polyunsaturate; HELP) contained a substantially greater proportion of erucic acid (54%) compared with high erucic rapeseed oil (46%). Although the total VLCFA content was greater in oil from HELP lines (64%) than from high erucic rapeseed (57%), analysis of triacylglycerol composition showed negligible incorporation of VLCFAs into the sn‐2 position. Rancimat analysis showed that the thermal stability of rapeseed oil was improved greatly as a consequence of reduction of PUFA content, from 3.8 and 4.2 h in conventional low erucic and high erucic rapeseed oils, respectively, to 11.3 and 16.4 h in high oleic low PUFA (HOLP) and HELP oils, respectively. Our results demonstrate that engineering of the lipid biosynthetic pathway of rapeseed, using traditional approaches, enables the production of renewable industrial oils with novel composition and properties.     

假丝酵母菌GXU08产脂肪酶发酵条件的优化

以假丝酵母菌GXU08产脂肪酶催化合成麝香类香料—环十五内酯目前已备受关注,在一定条件下,环十五内酯的转化率与脂肪酶的水解酶活有直接关系,酶活越高其催化合成环十五内酯的能力越强。通过单因素试验和正交试验,对假丝酵母菌GXU08产脂肪酶的发酵条件进行优化。结果表明:最佳发酵培养基配方为蔗糖0.5%,淀粉0.5%,蛋白胨1.5%,K_2HPO_40.05%,MgSO_40.15%,(NH_4)_2SO_41%,茶油1.5%,菜籽油1.5%,pH=8,此培养基在28℃,180 r/min的条件下发酵培养48h,脂肪酶水解活力达到27.53 U/mL,是初始发酵培养基条件下所得脂肪酶酶活的3.74倍;其环十五内酯的转化率为16.6%,是优化前的4倍。     

Solvent-free glycerolysis of sunflower oil and anchovy oil catalyzed by a 1,3-specific lipase

Solvent-free glycerolysis of sunflower oil catalyzed with lipase D Amano 100 gave the highest partial acylglycerols content at 40°C using an oil:glycerol molar ratio of 1:2 and 500 Units lipase/ g oil. After 6 h, the partial acylglycerols content of the reaction mixture was 53% (w/w). Glycerolysis of anchovy oil catalyzed under the same conditions gave a partial acylglycerols content of 47% (w/w) after 24 h.     

Lipase from marine Aspergillus awamori BTMFW032: production, partial purification and application in oil effluent treatment

Marine fungus BTMFW032, isolated from seawater and identified as Aspergillus awamori, was observed to produce an extracellular lipase, which could reduce 92% fat and oil content in the effluent laden with oil. In this study, medium for lipase production under submerged fermentation was optimized statistically employing response surface method toward maximal enzyme production. Medium with soyabean meal-0.77% (w/v); (NH(4))(2)SO(4)-0.1m; KH(2)PO(4)-0.05 m; rice bran oil-2% (v/v); CaCl(2)-0.05 m; PEG 6000-0.05% (w/v); NaCl-1% (w/v); inoculum-1% (v/v); pH 3.0; incubation temperature 35°C and incubation period-five days were identified as optimal conditions for maximal lipase production. The time course experiment under optimized condition, after statistical modeling, indicated that enzyme production commenced after 36 hours of incubation and reached a maximum after 96 hours (495.0 U/ml), whereas maximal specific activity of enzyme was recorded at 108 hours (1164.63 U/mg protein). After optimization an overall 4.6-fold increase in lipase production was achieved. Partial purification by (NH(4))(2)SO(4) precipitation and ion exchange chromatography resulted in 33.7% final yield. The lipase was noted to have a molecular mass of 90 kDa and optimal activity at pH 7 and 40°C. Results indicated the scope for potential application of this marine fungal lipase in bioremediation.     

Kinetic modeling of immobilized-lipase catalyzed transesterification of n-octanol with vinyl acetate in non-aqueous media

Organic esters are employed as solvents, fragrance, flavors, and precursors in a variety of industries. Particularly, aliphatic esters are greatly used in flavor industry, mainly as fixatives and modifiers, and aromatic esters in fragrance compositions. Esters are produced by a variety of methods among which esterification and transesterification with acid catalysts under reflux conditions are prominent. The use of biocatalysts provides an opportunity for carrying out reactions under milder conditions leading to better quality products suitable in fragrance and flavor industry. Transesterification of n-octanol with vinyl acetate was studied at 30 °C as a model reaction by employing different lipases as catalysts such as Psedomonas species lipase immobilized on diatomite, free Candida rugosa lipase. Novozym 435 (lipase B from Candida antarctica; immobilized on macro-porous polyacrylic resin beads) and Lipozyme IM 20 (Mucor miehei lipase immobilized on anionic resin). Novozym 435 was found to be the most active catalyst in heptane as a solvent. A conversion of 82% with 100% selectivity of n-octyl acetate was obtained at 30 °C in 90 min using equimolar quantities of the reactants with 0.833 g l⁻¹ of Novozym 435. Transesterification of other alcohols such as n-decanol, benzyl alcohol, cinnamyl alcohol, 2-ethyl-1-hexanol, 1-phenyl ethyl alcohol, and 2-phenyl ethyl alcohol was also studied with vinyl acetate. The analysis of the initial rate data and progress curve data showed that the reaction obeys the ternary complex bi–bi mechanism with inhibition by n-octanol. The experimental and theoretical values matched very well.

The order of transesterification reactivity of vinyl acetate with various alcohols in presence of Novozym 435 under otherwise identical conditions at 30 °C was found to be as follows:

n-octanol>n-decanol>benzylalcohol>cinnamylalcohol>2-ethyl-1-hexanol>2-phenylethylalcohol>1-phenylethylalcohol.

     

Effects of Rapeseed Oil on the Rhizodegradation of Polyaromatic Hydrocarbons in Contaminated Soil

Plants have the ability to promote degradation of polycyclic aromatic hydrocarbons (PAHs) in contaminated soil by supporting PAH degrading microorganisms in the rhizosphere (rhizodegradation). The aim of this study was to evaluate if rapeseed oil increases rhizodegradation because various studies have shown that vegetable oils are able to act as extractants for PAHs in contaminated soils and therefore might increase bioavailability of PAHs for microbial degradation. In this study different leguminous and grass species were tested. The results suggested a significant impact of vegetable oil (1 and 3% w/w) on plant growth (decrease of plant height and biomass). The results of the pot experiment showed a decrease in the PAH content of the soil without amendment of rapeseed oil after six months. In soil amended with 1% and 3% of oil, there was no decrease in PAH content within this period. Although no enhancement of PAH degradation by plants could be measured in the bulk soil of the pot experiments, a rhizobox experiment showed a significant reduction of PAH content in the rhizosphere of alfalfa (Medicago sativa cv. Europe). Our investigations also showed significant differences in the degradation behaviour of the 16 individually analysed PAHs.     

Lipase-catalyzed transesterification of rapeseed oils for biodiesel production with a novel organic solvent as the reaction medium

tert-Butanol, as a novel reaction medium, has been adopted for lipase-catalyzed transesterification of rapeseed oil for biodiesel production, with which both the negative effects caused by excessive methanol and by-product glycerol could be eliminated. Combined use of Lipozyme TL IM and Novozym 435 was proposed further to catalyze the methanolysis and the highest biodiesel yield of 95% could be achieved under the optimum conditions (tert-butanol/oil volume ratio 1:1; methanol/oil molar ratio 4:1; 3% Lipozyme TL IM and 1% Novozym 435 based on the oil weight; temperature 35 °C; 130 rpm, 12 h). There was no obvious loss in lipase activity even after being repeatedly used for 200 cycles with tert-butanol as the reaction medium. Furthermore, waste oil was also explored for biodiesel production and it has been found that lipase also showed good stability in this novel system.