Esterification of Short Chain Organic Acids with Alcohols by a Lipase Microencapsulated in Reversed Micelles

A Mucor miehei lipase was used to catalyse the esterification reaction between propionic acid and oleyl alcohol in reversed micelles of AOT in isooctane. Small-scale model studies were performed to study the influence of various parameters on the formation of oleyl propionate by this lipase. The maximum synthetic activity was obtained at w₀ = 4.0. At high temperatures (65°C) the enzyme displays a better stability for a low water content (w₀ = 3.3). The specificity of lipase was influenced by the solubilized water in the reversed micelles.     

Kinetics of lipase deactivation in AOT/isooctane reversed micelles

The stability of lipase in AOT/isooctane reversed micellar solution was investigated. It was found that the lipase deactivated to a stable state that was not completely inactivated. The lipase residual activity after achieving the stable state in AOT/isooctane reversed micelles at 30 °C, pH 7.0, W₀=8.0 was found to be 0.15, and the first-order deactivation rate coefficient of lipase at the same conditions was regressed to be 0.75 h⁻¹. The stability of lipase was increased while oleic acid was added. Assuming the protection of oleic acid to lipase stability is due to the lipase–oleic acid complex does not decay, the kinetic model of lipase deactivation in AOT/isooctane reversed micellar solution including the influence of oleic acid was established. It was shown with the model equation that the increase in stability of the enzyme by oleic acid could be quantitatively estimated by the dissociation constant of lipase–oleic acid complex which was determined by product inhibition experiments. The model equation fit the experimental data well with an average relative deviation of 3.40%.     

Lipase-catalyzed esterification of fatty acid in DMSO (dimethyl sulfoxide) modified AOT reverse micellar systems

AOT reverse micellar system was modified with DMSO for improved esterification activity of Chromobacterium viscosum lipase (glycerol-ester hydrolase, EC 3.1.1.3). The enzymatic activity was strongly affected by the concentration of DMSO, and maximum activity was obtained at 30-40 mM. The various relevant physical parameters such as w₀ (molar ratio of water to AOT), pH and reaction temperature that influence the activity of lipase were studied in order to obtain the best value and compared with those in simple AOT reverse micelles. The apparent activation energy decreased in the presence of DMSO. The stability of lipase entrapped in modified AOT systems was excellent, and the half-life was about 3.25 times than that observed in simple AOT systems at 25°C. A simple first-order deactivation model was considered to determine the deactivation rate constant. The thermodynamic stability of lipase in reverse micelles was measured by the Gibbs free energy. A fluorescence study was performed to provide information on structural changes in AOT reverse micelles which was accompanied by the addition of DMSO.     

Chemo-enzymatic epoxidation of oleic acid and methyl oleate in solvent-free medium

Chemo-enzymatic epoxidation of oleic acid (OA) and its methyl ester has been performed using hydrogen peroxide and immobilized lipase from Candida antarctica (Novozym® 435). The purpose of the study was to characterize the reaction under solvent-free conditions. The reaction temperature had a significant impact on epoxidation of OA. At lower temperatures, the substrate conversion was hindered by the formation of solid epoxystearic acid product. Nearly 90% conversion of OA to the epoxide product was obtained after 6 h at 50°C. Longer reaction times at 40°C and above resulted in by-product formation and eventually lowered the product yield. In contrast, the reaction with methyl oleate (MO) was less influenced by temperature. Almost complete epoxidation was achieved at 40-60°C; the higher the temperature the shorter was the reaction time. The main epoxidation product obtained was epoxystearic acid methyl ester (EME), and the remaining was epoxystearic acid (EA) formed by the hydrolytic action of the lipase. Recycling of the lipase for epoxidation of MO at 50°C indicated that the immobilized enzyme was prone to activity loss.     

Enzymatic and Non-Enzymatic Esterification of long Polyunsaturated Fatty Acids and Lysophosphatidylcholine in Isooctane

Phosphatidylcholine containing large amounts of long polyunsaturated fatty acid, eicosapentaenoic acid (C20:5) and docosahexaenoic acid (C22:6), was synthesized in isooctane. Immobilized phospholipase A₂ was used as a catalyst. A parallel non-enzymatic esterification reaction was investigated in separate experiments.

The concentrations of lyso-phosphatidylcholine, polyunsaturated fatty acids, water and the enzyme were varied over wide ranges as were the temperature and the reaction time. The type of enzyme, carrier and immobilization procedure were held constant.

The yield of phosphatidylcholine was relatively high (about 21%) when the concentration of polyunsaturated fatty acids was high (300 mg/g of reaction mixture) and the water content was low (below 30% of the dry immobilized enzyme). The highest yield of phosphatidylcholine was found at 80 hours and 75°C. However, at this temperature an extensive non-enzymatic reaction between polyunsaturated fatty acids and lyso-phosphatidylcholine occurred. At 80°C the polyunsaturated fatty acids were partly oxidized. Therefore, a temperature of 45°C to 65°C is probably the optimum temperature for the reaction.     

Lipase-Catalyzed Synthesis and Hydrolysis of Cholesterol Oleate in Aot/Isooctane Microemulsions

We have examined a lipase-catalyzed bidirectional ester synthesis/hydrolysis reaction in a water-in-oil microemulsion system. The reactants were cholesterol (alcohol), oleic acid (acid) and cholesterol oleate (ester), and the solvent system consisted of sodium bis(2-ethylhexyl)sulfosuccinate (AOT)/isooctane/water. The reactions were assayed by using [³H]oleic acid, [³H]cholesterol, or [³H]cholesterol oleate for the synthesis and hydrolysis reactions, respectively (separate incubations). The lipase that we used derived from Candida cylindracea, and was used at a concentration of 0.1mg/ml microemulsion. The reactions were performed at 22°C as the reactions proceeded more slowly at higher temperatures. With the initial reactant concentrations set to 10 mM cholesterol, 1 min oleic acid, and 1 mM cholesterol oleate, it was observed that the optimal [H₂O]/[AOT] ratio was at about 9 both for the esterification reaction and for the hydrolysis reaction (after 24 h). The hydrolysis reaction was slower than the synthesis reaction at all [H₂O]/[AOT] ratios studied (0-20), but the difference in reaction yield for the synthesis and the hydrolysis reactions became smaller as the reaction time increased (up to 11 days). When the reaction yield was followed as a time function, it was observed that about 80% of the oleic acid was esterified within 3 days of reaction ([H₂O]/[AOT] ratio of 6), whereas the corresponding value of 80% hydrolysis of cholesterol oleate was reached within 11 days. The results of the present study indicate that by choosing optimal reactant concentrations and reaction conditions, it is at least in part possible to determine the direction of the lipase-catalyzed synthesis/hydrolysis reaction.     

Enhanced activity and stability of immobilized lipases by treatment with polar solvents prior to lyophilization

Lipases from Candida rugosa, Mucor javanicus and Rhizopus oryzae were respectively adsorbed on Amberlite XAD-7 followed by incubation in 2-propanol and then lyophilization. The activities of the immobilized enzymes were 1.6–3.4 times higher than those of the immobilized enzymes without incubation in the organic solvent before lyophilization for esterification of lauric acid (0.1 M) and 1-propanol (0.1 M) in isooctane at 37 °C. The immobilized C. rugosa lipase (Sigma) without the incubation did not show any activity but displayed considerable activity (19.8 μmol h⁻¹ mg⁻¹) after the incubation before lyophilization. Besides 2-propanol, acetone, 1-propanol and ethyl acetate were also found to be good solvents for treating M. javanicus lipase immobilized on Amberlite XAD-7 and acetone was the best among them. When incubated in isooctane at 25 °C for 120 h, the immobilized M. javanicus lipase prepared by incubation in acetone for 1 h before lyophilization retained 70% of its initial activity while the immobilized enzyme without the solvent treatment kept only 50% of its initial activity.     

Kinetic characterisation of enzymatic esterification in a solvent system: adsorptive control of water with molecular sieves

The kinetics of enzymatic esterification of glycerol with oleic acid, in equimolar ratio, catalyzed by immobilized Mucor miehei lipase in a solvent system in the presence of the molecular sieves was carried out at 37°C at different Lipozym and solvent (n-hexane) concentrations and the molecular sieve contents were studied in a batch stirred-tank reactor (BSTR). The reactions were followed by the determination of reaction conversions during 45 h. The experimental data of enzymatic esterification of glycerol with oleic acid in a solvent system in the presence of molecular sieves showed minimal deviation from the calculated value in the irreversible second order kinetic model. On the basis of the experimental data, we found an empirical correlation between concentrations of Lipozym, concentrations of solvent (n-hexane), contents of the molecular sieve and the reaction rate constant, k₁.     

Continuous glycerolysis of olive oil by Chromobacterium viscosum lipase immobilized in liposome in reversed micelles

Chromobacterium viscosum lipase which has adsorbed on liposome and solubilized in microemulsion droplets of glycerol containing a little amount of water could catalyze the glycerolysis of olive oil. Studies on the continuous glycerolysis of olive oil by the immobilized enzyme was done at 37 degrees C in continuous stirred vessel bioreactor with polysulfone membrane. The effect of the flow rate of substrate (olive oil) in isooctane on the conversion and composition of the outlet was investigated using high-performance liquid chromatography (HPLC). The conversion increased with decrease in the flow rate. And we studied the effect of water content in the glycerol-water-lipase solution on the glycerolysis reaction. The conversion to desirable products, mono- and di-olein, was improved without a substantial production of oleic acid at lower water concentrations, i.e., below 8.0% (w/v) which corresponds to a w(o) value of 0.97. At water concentration higher than 8.0% (w/v), the amount of free fatty acid was dramatically increased. Higher operational stability of the enzyme reactor, and the half-line of the enzyme continuous reaction was about 7 weeks.     

Lipase-catalyzed hydrolysis of olive oil in chemically-modified AOT/isooctane reverse micelles in a hollow fiber membrane reactor

The hydrolysis of olive oil catalyzed by Candida rugosa lipase in sodium bis(2-ethylhexyl)sulfosuccinate (AOT)/isooctane and the synthetic sodium bis(2-ethylhexyl polyoxyethylene)sulfosuccinate (MAOT)/isooctane reverse micellar systems was investigated in a polysulfone hollow fiber membrane reactor with recycle of the reaction mixture. Lipase was completely retained by the membrane while olive oil and oleic acid freely passed through. The retention of reverse micelles depended on W ₀ (molar ratio of water to surfactant). At an olive oil concentration of 0.23 mol l^–1 the final substrate conversion in the MAOT micellar system was about 1.4 times of that in the AOT micellar system.     

Comparative Studies of Lipase from Rhizopus Delemar in Various Microemulsion Systems

Hydrolysis of triglycerides by lipase from Rhizopus delemar has been studied in three different types of microemulsion systems. Microemulsions were prepared by using anionic (AOT), cationic (CTAB) and nonionic (C₁₂E₄) surfactants. Various parameters affecting the reaction, such as temperature, pH optimum, water content (R = [H₂O]/[surfactant]), as well as K_m.app and V_app, were determined using triolein and tributyrin as substrates. Maximum enzyme activity was obtained at R = 9, T = 30°C and pH = 6.5 in anionic surfactant systems, while in cationic, it was found at R = 7, T = 22.5°C and pH = 5.8. The stability of the enzyme was also studied in anionic and cationic systems under various conditions. The enzymatic reaction was also found to be very slow when it was studied in the C₁₂E₄ systems.     

Operational stability of Brevibacterium imperialis CBS 489-74 nitrile hydratase

Brevibacterium imperialis CBS 489-74 was grown in broths prepared with yeast and malt extract, bacteriological peptone and 2% glucose or differently modified with the addition of Na-phosphate buffer, FeSO₄, MgSO₄ and CoCl₂. The peak production of nitrile hydratase (NHase) did not change significantly. At the stationary growth phase, the units per milliliter of broth (60 units ml⁻¹) were more important than those at the exponential growth phase.

The NHase operational stability of whole resting cells was monitored following the bioconversion of acrylonitrile to acrylamide in continuous and stirred UF-membrane reactors. The rate of inactivation was independent on buffer molarity from 25 to 75 mM and on pH from 5.8 to 7.4. Enzyme stability and activity remained unchanged in distilled water. The initial reaction rate increased from 12.8 to 23.8 g acrylamide/g dry cell/h, but NHase half-life dropped from 33 to roughly 7 h when temperature was varied from 4°C to 10°C. The addition of butyric acid up to 20 mM did not improve enzyme operational stability, and largely reduced (94%) enzyme activity. Acrylonitrile caused an irreversible damage to NHase activity. High acrylonitrile conversion (86%) was attained using 0.23 mg cells/ml in a continuously operating reactor.     

Enzymatic Synthesis of Ethyl-glucoside Monooleate with Lipase in Solvent-free Medium

Ethylglucoside monooleate was synthesized by esterification between ethylglucoside and oleic acid with immobilized lipase from Candida antarctica in a solvent-free system. It was shown that a stirred tank reactor was suitable for the enzymatic reaction process involving substrates with low miscibility, in which the biocatalyst was recycled five times without significant activity loss. Removal of the co-product, water, from the reaction medium by carrying out the reaction under reduced pressure benefited the esterification reaction and increased the monooleate yield up to 97% within 8 hours.     

Enzymatic interesterification of triglyceride with surfactant-coated lipase in organic media

Several surfactant-coated enzymes have been prepared by coating lipases of various origins with a nonionic surfactant, glutamic acid dioleylester ribitol (2C(18)Delta(9)GE). Enzymatic interesterification of tripalmitin with oleic acid using the surfactant-coated lipase was carried out in organic media. The surfactant-coated lipases could effectively catalyze the interesterification of glycerides better than did the powder lipases. A suitable organic solvent was an aliphatic hydrocarbon such as isooctane. The enzymatic activity for the interesterification strongly depended on the origin of the lipase. The surfactant-coated lipase prepared by Mucor javanicus showed the highest enzymatic activity for the interesterification of glycerides, although its powder lipase did not show enzymatic activity. Selective interesterification of glycerides could be performed by adjusting the concentration ratio of oleic acid to tripalmitin in isooctane. Di-substituted glyceride could be selectively produced when the concentration ratio of carboxylic acid to glycerides was 7. (c) 1995 John Wiley & Sons, Inc.     

Morphological, biochemical and kinetic properties of lipase from Candida rugosa immobilized in zirconium phosphate

Zirconium phosphate (ZrP), a low-cost inorganic material with well-defined physicochemical properties, was successfully used as support for immobilizing Candida rugosa lipase by covalent bonding. The immobilized derivative showed high catalytic activity in both aqueous and non-aqueous media. Fourier transform infrared spectroscopy, X-ray diffraction, and scanning electron microscopy measurements demonstrated that the ZrP fulfilled the morphological requirements for use as a matrix for immobilizing lipases. The free and immobilized lipases were compared in terms of pH, temperature and thermal stability. The immobilized lipase had a higher pH optimum (7.5) and higher optimum temperature (50°C) than the free lipase. Immobilization also increased the thermal stability. The hydrolysis of p-nitrophenyl palmitate (pNPP) by immobilized lipase, examined at 37°C, followed Michaelis-Menten kinetics. Values for K_m=1.18 µM and V_max=325Umg^-1 indicated that the immobilized system was subject to mass transfer limitations. The immobilized derivative was also tested under repetitive reaction batches in both ester hydrolysis and synthesis.     

Optimization of lipase-catalyzed glucose fatty acid ester synthesis in a two-phase system containing ionic liquids and t-BuOH

Selective lipase-catalyzed synthesis of glucose fatty acid esters in two-phase systems consisting of an ionic liquid (1-butyl-3-methyl imidazolium tetrafluoroborate [BMIM][BF₄] or 1-butyl-3-methyl imidazolium hexafluorophosphate [BMIM][PF₆]) and t-butanol as organic solvent was investigated. The best enzyme was commercially available lipase B from Candida antarctica (CAL-B), but also lipase from Thermomyces lanuginosa (TLL) gave good conversion. After thorough optimization of several reaction conditions (chain-length and type of acyl donor, temperature, reaction time, percentage of co-solvent) conversions up to 60% could be achieved using fatty acid vinyl ester as acyl donors in [BMIM][PF₆] in the presence of 40% t-BuOH with CAL-B at 60 °C.     

Synthesis of N-Octyl Oleate with Lipase from Mucor miehei Immobilized onto Polyethylene Based Graft Copolymers

Lpase from Mucor miehei was immobilized onto partially hydrolyzed poly(ethylene)-g.co-hydroxyethyl methacrylate (PE/HEMA) via spacer arms of 1,6-diaminohexane and glutaraldehyde-. The PE/HEMA-lipase system was used for the enzymatic esterification of n-octanol with oleic acid in the absence of organic solvents. The influence of lipase' concentration, in the attachment solution, on the ester production profile and initial reaction rate was studied. It was found that very small amounts of lipase gave preparations which reached good degrees of conversion. The effect of the initial oleic acid concentration on that pseudo-first order reaction, as well as the presence of water in the reactional medium and the influence of temperature were evaluated. It was found that initial oleic acid concentrations lesser than 1.2 M did not inhibit the immobilized lipase activity; the presence of small amount of water (10–30μ) solubilized in the reaction mixture (6.5 cm³) increased the lipase activity and a maximum of activity of the immobilized lipase preparation was found at 55d`C. The operational stability of the preparation was determined at 37d`C in a BSTR type reactor and a half-life time of three days for the immobilized lipase was obtained.     

Studies on synthesis of short chain alkyl esters catalyzed by goat pregastric lipase

Goat pregastric lipase, in the form of a suspended enzyme powder, was found to be active in catalyzing the synthesis of alkyl esters in anhydrous organic solvents. The rate of catalyzed synthesis of esters was very dependent on the solvent medium, and maximum activity was found when a hydrocarbon was used as the solvent. The optimal temperature for the catalyzed synthesis ranged from 30 to 40°C and the maximal temperature was 35°C for the synthesis of butyl caproate in isooctane. The selectivity for the carbon-chain length of the fatty acid by the lipase was similar to that seen in hydrolysis reactions in aqueous solution, and the optimal rate of synthesis of alkyl esters was found for synthesis of the esters which had 8 or 10 carbons in the alkyl moieties from the two individual substrates. The rate of synthesis was also dependent on the water content in the system, with maximum activity occurring at 1% w/w water in isooctane.     

Solid substrate cultivation of Gibberella fujikuroi on an inert support

Growth of Gibberella fujikuroi on Amberlite, an inert support, and gibberellic acid (GA₃) production was studied in glass columns under different conditions of temperature and water activity (a_w). Maximum biomass concentration and GA₃ production were respectively 40 (mg/g inert support) and 0.73 (mg/g inert support). While high specific growth rates were obtained, low initial nitrogen resulted in low biomass concentrations. Maximum GA₃ (31°C, a_w=0.985) was not produced by the maximum concentration of biomass (25°C, a_w=0.992). Peaks in the rate curves of either outlet gas, CO₂ or O₂, occurred on exhaustion of urea indicating, for future works, just when to feed the culture additional nitrogen.     

'P' solubilization potential of plant growth promoting Pseudomonas mutants at low temperature

Pseudomonas fluorescens strain GRS₁, PRS₉ and their cold tolerant mutants were examined for their tricalcium phosphate (TCP) solubilizing activity in NBRIP (broth) media at 10°C and 25°C. Invariably, all the cold tolerant mutants of GRS₁ and PRS₉ were found more efficient than their respective wild type counterparts for ‘P’ solubilization activity at 10°C as compared to 25°C. ‘P’ solubilization potential of CRM was found maximum among all the strains followed by CRPF₆ and CRPF₄. To the best of out knowledge, this is the first report regarding low temperature ‘P’ solubilization activity.