Lipase immobilisation: an equilibrium study of lipases immobilised on hydrophobic and hydrophilic/hydrophobic supports

This work investigates the enzyme-support equilibrium behaviour in immobilised lipase biocatalysts. Equilibrium data determines the maximum enzyme up-take by unit weight of support. Four lipases were immobilised on two polymeric supports, respectively. They were Lipase PS from Pseudomonas, Lipolase 100L from Humicola, SP871 from Rhizomucor miehel and QL from Alcaligenes. The supports were Accurel EP100 (a polypropylene material) and 45SAA (a polypropylene/silica composite). Experimentally, equilibrium was expressed in terms of lipase loading (LU/g support) versus residual lipase concentration (LU/dm³). Activity, efficiency and operational stability of the immobilised lipases were assayed by solvent-free esterification of oleic acid and octanol.Equilibrium data were modelled by the Langmuir, Freundlich and Redlich–Peterson formulae. It was found that Lipolase 100L/Accurel, PS/45SAA and SP871/45SAA systems conformed to the Langmuir behaviour, while Lipase PS/Accurel and SP871/Accurel systems followed the Freundlich behaviour and Lipolase 100L/45SAA, QL/45SAA and QL/Accurel EP100 resembled Redlich–Peterson behaviour. Whereas immobilisation on Accurel EP100 resulted in classical equilibrium isotherms with all four lipases, immobilisation on support 45SAA resulted in two-plateau equilibrium curves which included a step change in the isotherm for all lipases studied, except for SP871. Quantitatively, for 1 g lipase, Accurel and 45SAA had a maximum capacity of 140 and 260 kLU for PS, 112 and 550 kLU for Lipolase 100L, 320 and 800 kLU for SP871 and 18 and 29 kLU for QL, respectively.     

Improved stability and reactivity of Fusarium solani cutinase in supercritical CO2

Cutinase from Fusarium solani pisi was immobilized on Accurel EP100 and catalyzed the esterification of hexanoic acid with hexanol in supercritical CO. The enzyme lost only 10% of its activity over six days. Esterification was maximal with a water activity of a = 0.76.     

Role of the support surface on the loading and the activity of Pseudomonas fluorescens lipase used for biodiesel synthesis

The present work investigates the influence of the support surface on the loading and the enzymatic activity of the immobilized Pseudomonas fluorescens lipase. Different porous materials, polypropylene (Accurel), polymethacrylate (Sepabeads EC-EP), silica (SBA-15 and surface modified SBA-15), and an organosilicate (MSE), were used as supports. The immobilized biocatalysts were compared towards sunflower oil ethanolysis for the sustainable production of biodiesel. Since the supports have very different structural (ordered hexagonal and disordered) and textural features (surface area, pore size, and total pore volume), in order to consider only the effect of the support surface, experiments were performed at low surface coverage. The different functional groups occurring on the support surface allowed either physical (Accurel, MSE, and SBA-15) or chemical adsorption (Sepabeads EC-EP and SBA-15–R-CHO). The surface-modified SBA-15 (SBA-15–R-CHO) allowed the highest loading. The lipase immobilized on the MSE was the most active biocatalyst. However, in terms of catalytic efficiency (activity/loading) the lipase immobilized on the SBA-15, the support that allowed the lowest loading, was the most efficient.     

Selection of CalB immobilization method to be used in continuous oil transesterification: analysis of the economical impact

Enzymatic transesterification of triglycerides in a continuous way is always a great challenge with a large field of applications for biodiesel, bio-lubricant, bio-surfactant, etc. productions. The lipase B from Candida antarctica (CalB) is the most appreciated enzyme because of its high activity and its non-regio-selectivity toward positions of fatty acid residues on glycerol backbone of triglycerides. Nevertheless, in the field of heterogeneous catalysis, we demonstrated that the medium hydrophilic nature of the support used for its commercial form (Lewatit VPOC1600) is a limitation. Glycerol is adsorbed onto support inducing drastic decrease in enzyme activity. Glycerol would form a hydrophilic layer around the enzyme resulting in diffusional limitations during triglyceride transfer to the enzyme. Accurel MP, a very hydrophobic macroporous polymer of propylene, was found not to adsorb glycerol. Immobilization conditions using this support were optimized. The best support was Accurel MP1001 (particle size<1000 μm) and a pre-treatment of the support with acetone instead of ethanol enables the adsorption rate and the immobilized enzyme quantity to be maximized. An economical approach (maximization of the process net present value) was expanded in order to explore the impact of immobilization on development of an industrial packed bed reactor. The crucial ratio between the quantity of lipase and the quantity of support, taking into account enzyme, support and equipped packed bed reactor costs was optimized in this sense. The biocatalyst cost was found as largely the main cost centre (2-10 times higher than the investments for the reactor vessel). In consequence, optimal conditions for immobilization were a compromise between this immobilization yield (90% of lipase immobilized), biocatalyst activity, reactor volume and total investments.     

Sol-gel powders and supported sol-gel polymers for immobilization of lipase in ester synthesis

Candida rugosa lipase was entrapped in hybrid organic–inorganic sol-gel powder prepared by acid-catalyzed polymerization of tetramethoxysilane (TMOS) and alkyltrimethoxysilanes, and used in catalyzing esterification reactions between ethanol and butyric acid in hexane. Optimum preparation conditions were studied, which are gels made from propyltrimethoxysilane (PTMS)/TMOS molar ratio=4:1, hydrolysis time of silane precursor=30 min, water/silane molar ratio=24, enzyme loading=6.25% (w/w) of gel, and 1 mg PVA/mg lipase. The percentage of protein immobilization was 95% and the resulting lipase specific activity was 59 times higher than that of a non-immobilized lyophilized lipase. To prepare magnetic lipase-immobilized sol-gel powder (MLSP) for easier recovery of the biocatalyst, Fe₃O₄ nanoparticles were prepared and co-entrapped with lipase during gel formation. This procedure induced surface morphological change of the sol-gel powder and showed adverse effect on enzyme activity. Hence, although only 9% decrease in protein immobilization efficiency was observed, the corresponding reduction in enzyme activity could be up to 45% when sol-gel powder was doped with 25% (v/v) Fe₃O₄ magnetic nanoparticles solution. Lipase-immobilized sol-gel polymer was also formed within the pores of different porous supports to improve its mechanical stability. Non-woven fabric, with a medium pore size of all the supports tested, was found to be the best support for this purpose. The thermal stability of lipase increased 55-fold upon entrapment in sol-gel materials. The half-lives of all forms of sol-gel-immobilized lipase were 4 months at 40 °C in hexane.     

Bioconversion of phospholipids by immobilized phospholipase A2

Phospholipase A₂ selectively hydrolyses the ester linkage at the sn-2 position of phospholipids forming lysocompounds. This bioconversion has importance in biotechnology since lysophospholipids are strong bioemulsifiers. The aim of the present work was to study the kinetic behaviour and properties of immobilized phospholipase A₂ from bee venom adsorbed into an ion exchange support. The enzyme had high affinity for CM-Sephadex^® support and the non-covalent interaction was optimum at pH 8. The activity of immobilized phospholipase A₂ was comparatively evaluated with the soluble enzyme using a phospholipid/Triton X-100 mixed micelle as assay system. The immobilized enzyme showed high retention activity and excellent stability under storage. The activity of the immobilized system remained almost constant after several cycles of hydrolysis. Immobilized phospholipase A₂ was less sensitive to pH changes compared to soluble form. The kinetic parameters obtained (V_max 883.4 μmol mg⁻¹ min⁻¹ and a K_m 12.9 mM for soluble form and V_max = 306 μmol mg⁻¹ min⁻¹ and a K_m = 3.9 for immobilized phospholipase A₂) were in agreement with the immobilization effect. The results obtained with CM-Sephadex^®-phospholipase A₂ system give a good framework for the development of a continuous phospholipid bioconversion process.     

Response surface modelling of the production of ω-3 polyunsaturated fatty acids-enriched fats by a commercial immobilized lipase

The aim of this study was to model the production of fats, enriched with ω-3 polyunsaturated fatty acids (ω-3 PUFA) for nutraceutical purposes, via the response surface methodology. These fats were obtained by transesterification of palm oil stearin (POS) with a concentrate (EPAX 2050TG) of triglycerides enriched with ω-3 PUFA and soybean oil, catalysed by a commercial immobilized Candida antarctica lipase (“Novozym 435”).

The initial water activity (a_w) of the biocatalyst, POS and EPAX 2050TG concentrations, time and temperature showed a significant effect on the transesterification reaction, as well as on the competing reactions of hydrolysis and lipid oxidation.

Depending on the factors included, the transesterification reaction was described either by first- or second-order models.

The production of free fatty acids, which is ascribed both to the hydrolytic reaction and the mechanism of lipase-catalysed transesterification, showed a second-order dependence on the initial a_w of the biocatalyst.     

Involvement of prostaglandin E receptor EP3 subtype in duodenal bicarbonate secretion in rats

We investigated the involvement of prostaglandin E (PGE) receptor subtype EP3 in the regulatory mechanism of duodenal HCO₃⁻ secretion in rats. A proximal duodenal loop or a chambered stomach was perfused with saline, and HCO₃⁻ secretion was measured using a pH-stat method and by adding 2 mM HCl. Mucosal acidification was achieved through 10 min of exposure to 10 mM HCl in the duodenum or 100 mM HCl in the stomach. Various EP agonists or the EP4 antagonist were given i.v., while the EP1 or EP3 antagonist was given s.c. or i.d., respectively. Sulprostone (EP1/EP3 agonists) stimulated duodenal HCO₃⁻ secretion in a dose-dependent manner, and this response was inhibited by AE5-599 (EP3 antagonist) but not AE3-208 (EP4 antagonist). AE1-329 (EP4 agonist) also increased duodenal HCO₃⁻ secretion, and this action was inhibited by AE3-208 but not AE5-599. The response to PGE₂ or acidification in the duodenum was partially attenuated by AE5-599 or AE3-208 alone but completely abolished by the combined administration. Duodenal damage caused by mucosal perfusion with 150 mM HCl for 4 h was worsened by pretreatment with AE5-599 and AE3-208 as well as indomethacin and further aggravated by co-administration of these antagonists. Neither the EP3 nor EP4 antagonist had any effect on the gastric response induced by PGE₂ or acidification. These results clearly demonstrate the involvement of EP3 receptors, in addition to EP4 receptors, in the regulation of duodenal HCO₃⁻ secretion as well as the maintenance of the mucosal integrity of the duodenum against acid injury.     

Recombinant Candida rugosa lipase 2 from Pichia pastoris: immobilization and use as biocatalyst in a stereoselective reaction

The characterization of the recombinant Candida rugosa Lip2 (r-Lip2) isoenzyme obtained from fed-batch cultures of Pichia pastoris under PAOX promoter was carried out, determining the optimal pH and temperature as well as their catalytic performance in both hydrolysis and synthesis reactions comparing with purified native Lip2 (n-Lip2) previously determined. The substrate specificity of r-Lip2 in hydrolysis reactions was determined with a series of triacylglycerols and p-nitrophenyl esters of variable acyl chain length. r-Lip2 showed the maximum specificity for both substrates towards medium-chain esters (C-8), similar behavior was observed with n-Lip2. However, significant differences were observed towards unsaturated substrates (triolein) or short-chain esters. A statistical design applied to study the effect of pH and temperature on lipase stability shown that r-Lip2, like n-Lip2, was more sensitive to pH than temperature changes. Nevertheless, the overall stability of soluble r-Lip2 was lower than soluble n-Lip2. The stability of r-lip2 was significantly improved by immobilization onto EP100, an excellent support for lipases with yields around 95% for offered lipolytic activity lower than 600 AU/mL. Finally, immobilized r-Lip2 was tested in the resolution of ibuprofen in isooctane by means of enantioselective esterification using 1-butanol as esterifying agent. r-Lip2 showed a better performance in terms of enantiomeric excess (74%) and enatiomeric factor (96%) than n-Lip2 (56 and 80%, respectively) for the same conversion (40%). Thus, r-Lip2 should be considered a good and pure biocatalyst, easy to produce and with a remaining activity of ca. 90% after one reaction cycle when immobilized on EP100.     

Immobilisation of lipases by adsorption and deposition: high protein loading gives lower water activity optimum

Two different immobilisation techniques for lipases were investigated: adsorption on to Accurel EP-100 and deposition on to Celite. The specific activities were in the same order of magnitude, 2.9 (mol min^–1 mg protein) when Celite was used as support and 2.3 (mol min^–1 mg^–1 protein) when Accurel EP-100 was used as support, even if the amount of lipase loaded differed by 2 orders of magnitude. Immobilisation on Accurel EP-100 was the preferred technique since 40–100 times more protein can be loaded/per g carrier, thus yielding a more active catalyst. The water activity profiles in lipase catalysed esterification were influenced by the amount of protein adsorbed to Accurel EP-100. Higher protein loading (40 mg g^–1) resulted in a bell-shaped water activity profile with highest specific activity (6.1 mol min^–1 mg^–1 protein) at a _w=0.11, while an enzyme preparation with low protein loading (4 mg g^–1) showed highest specific activity at a _w=0.75.     

Effect of serum concentration on retroviral vector production from the amphotropic ψCRIP murine producer cells

The production of ethanol by Saccharomyces cerevisiae immobilized cells and its esterification with oleic acid, catalysed by a lipase from Rhizomucor miehei, was the biochemical process considered as model to illustrate the concept of extractive biocatalysis. The selection of the most suitable support for lipase immobilization was carried out. The best results for the ethanol/oleic acid esterification reaction were obtained with the lipase adsorbed on a polyamide type support, Accurel EP 700. The immobilization method was optimized in terms of immobilization pH, contact time and protein/support ratio. The better performances of the extractive fermentations of ethanol were obtained when entrapped k-carrageenan Saccharomyces cerevisiae cells and a lipase from Rhizomucor miehei, free or immobilized in Accurel EP 700, were used simultaneously. The observed reutilization capacity of the immobilized enzyme could be advantageous for its application in a continuous reactor.     

Hydrogen peroxide degradation by immobilized cells of alkaliphilic Bacillus halodurans

Whole cells of Bacillus halodurans LBK 261 were used as a source of catalase for degradation of hydrogen peroxide. The organism, B. halodurans grown at 55°C and pH 10, yielded a maximum catalase activity of 275 U g^-1 (wet wt.) cells. The catalase in the whole cells was active over a broad range of pH with a maximum at pH 8-9. The enzyme was optimally active at 55°C, but had low stability above 40°C. The whole cell biocatalyst exhibited a K_m of 6.6 mM for H₂O₂ and V_max of 707 mM H₂O₂ min^-1 g^-1 wet wt. cells, and showed saturation kinetics at 50 mM H₂O₂. The cells were entrapped in calcium alginate and used for H₂O₂ degradation at pH 9 in batch and continuous mode. In the batch process, the immobilized preparation containing 1.5 g (wet wt.) cells could be recycled at least four times for complete degradation of the peroxide in 50 mL solution at 25°C. An excess of immobilized biocatalyst could be used in a continuous stirred tank reactor for an average of 9 days at temperatures upto 55°C, and in a packed bed reactor (PBR) for 5 days before the beads started to deform.     

The radiation crosslinked films based on PLLA/PDLA stereocomplex after TAIC absorption in supercritical carbon dioxide

The absorption of triallyl isocyanurate (TAIC) to equimolar stereo blends of PLLA and PDLA (sb-PLA samples) with crosslinker (TAIC) was controlled by supercritical carbon dioxide (sc-CO₂) treatment. The well-mixed sb-PLA/TAIC (sc-PLA) samples containing certain ratios of TAIC were obtained after vacuum evaporation. The sc-PLA samples were become much softer by sc-CO₂ treatment. The crosslinked sc-PLA materials with different crosslinking density were prepared by irradiation treatment at different radiation doses. Gel fraction, thermal properties and mechanical properties of crosslinked samples were investigated with different sc-PLA samples irradiated at the same radiation dose of 30 kGy and sc-PLA3 irradiated at different radiation doses. The crosslinking network inhibited crystallization, and enhanced the rigidity as well as lowered brittleness of irradiated samples. Although tensile strength and Young’s modulus of sc-PLA are reduced by sc-CO₂ treatment, they are much improved by radiation crosslinking at a suitable dose and the crosslinked samples become harder and tougher. The typical crosslinked obtained from sc-PLA3 irradiated at 30 kGy reveals the best thermal stability with the improved mechanical properties.     

Influence of different silica derivatives in the immobilization and stabilization of a Bacillus licheniformis protease (Subtilisin Carlsberg)

Alcalase 2T, a commercial preparation of Subtilisin Carlsberg, was covalent immobilized onto physiochemically characterized silica supports. The effect of mean pore diameter and surface chemistry on enzyme activity in the hydrolysis of casein has been examined. Two sets of chemically distinct silica supports were used presenting terminal amino (S_APTES) or hydroxyl groups (S_TESPM-pHEMA). The percentage of immobilized protein was smaller in S_APTES (31–39%) than in S_TESPM-pHEMA (62–71%), but presented higher total and specific activity. Silicas with large pores (S₁₀₀₀, 130/1200 Å) presented higher specific activities relative to those with smaller pore sizes (S₃₀₀, 130/550 Å). The influence of glutaraldehyde concentration and the time of enzyme coupling to the S₁₀₀₀S_APTES supports was examined. The apparent K_m value for the S₁₀₀₀S_APTES immobilized enzyme is lower than the soluble one which may be explained by the partitioning effects of the substrate. No intraparticle diffusion limitations were observed for the immobilized enzyme and therefore the substrate diffusion does not influence the observable kinetics. Finally, the optimum pH, optimum temperature, thermal stability, operational stability, and storage stability of the immobilized and freely soluble enzymes were compared.     

Stabilization of quaternary structure and activity of bovine liver catalase through encapsulation in liposomes

Bovine liver catalase was encapsulated in an aqueous phase of the phospholipid vesicle (liposome) to improve the stability of its tetrameric structure and activity. The catalase-containing liposomes (CALs) prepared were 30, 50 and 100 nm in mean diameters (CAL₃₀, CAL₅₀ and CAL₁₀₀, respectively). The CAL₁₀₀ included the types I, II and III based on the amounts of catalase encapsulated. The CAL₃₀, CAL₅₀ and CAL₁₀₀-I contained one catalase molecule per liposome, and the CAL₁₀₀-II and CAL₁₀₀-III on average 5.2 and 17 molecules, respectively. The storage stability of catalase in either CAL system was significantly increased compared to that of free catalase at 4 °C in a buffer of pH 7.4. At 55 °C, free catalase was much more deactivated especially with decreasing its concentration predominantly due to enhanced dissociation of catalase into subunits while it was so done at excessively high enzyme concentration mainly due to enhanced formation of catalase intermolecular aggregates. Among the three types of CAL₁₀₀, the CAL₁₀₀-II showed the highest thermal stability, indicating that an excess amount of catalase in the CAL₁₀₀-III was also disadvantageous to maintain an active form of the catalase even in liposome. In the CAL₁₀₀-III, however, the stability of catalase was significantly improved compared to that of free catalase at the same concentration. The CAL thermal stability was little affected by the liposome size as observed in the CAL₃₀, CAL₅₀ and CAL₁₀₀-I. An intrinsic tryptophan fluorescence of the catalase recovered from the CAL₁₀₀-II thermally treated at 55 °C revealed that a partially denatured catalase molecule was stabilized through its hydrophobic interaction with liposome membrane. This interaction depressed not only dissociation of catalase into subunits but also formation of an inactive intermolecular aggregate between the catalase molecules in a liposome. Furthermore, either type of CAL₁₀₀ showed a higher stability than free catalase in the successive decompositions of 10 mM H₂O₂ at 25 °C mainly because the H₂O₂ concentration was kept low inside liposomes due to the permeation barrier of the lipid membrane to H₂O₂.     

An efficient system for catalyzing ester synthesis using a lipase from a newly isolated Burkholderia cepacia strain

The synthesis of ethyl-oleate by the lipase from the newly isolated strain Burkholderia cepacia LTEB11 in three different systems has been studied - immobilization on a hydrophobic support (Accurel EP 100®), encapsulation in reverse micelles, and direct addition of powdered free enzyme to the reaction medium. The immobilized enzyme performed best, giving a 70% ester yield in 10 h, this yield being five-fold greater than that obtained for reversed micelles, and two and a half times greater than that obtained for direct addition. An increase in the amount of immobilized enzyme preparation added gave a 100% ester yield in 3 h. The immobilized preparation was quite stable, giving a 100% yield of ethyl-oleate during 11 repeated reactions, and 50% yield after 24 reactions. These results suggest that the lipase of our strain of B. cepacia LTEB11 immobilized on Accurel has good potential for application in biocatalysis in organic media.     

Activity and stability of chemically modified Candida antarctica lipase B adsorbed on solid supports

The effect of various covalent chemical modifications on the transesterification activity and stability of adsorbed lipase B from Candida antarctica (CALB) was studied in 2-butanone and o-xylene. CALB species modified with either polyethylene glycol 2000 monomethyl ether (MPEG), polyethylene glycol 300 mono-octyl ether (OPEG) or n-octanol (OCT) were used in combination with a hydrophobic (Accurel) and a hydrophilic (Duolite) support. The thermostabilities of adsorbed CALB in both solvents, and that of free CALB in o-xylene were not influenced by the modifications. In contrast, the thermostability of free CALB in 2-butanone decreased 2.5-fold after MPEG modification and increased 1.5-fold after modification with OPEG and n-octanol, compared to that of native CALB. The activities of the native and modified CALB species were up to 9-fold higher after adsorption onto Accurel than those of the corresponding free enzymes. Adsorption of these enzyme species onto Duolite only resulted in a 2- to 3-fold increase in the activity of OPEG- and OCT-modified CALB. The modified CALB species adsorbed onto Accurel show similar or up to 2-fold lower activities than do native adsorbed CALB species, while 1.5- to 6-fold higher activities were found for modified CALB species adsorbed onto Duolite. We propose that hydrophobic modifiers induce conformational changes of CALB during adsorption on a hydrophobic support whereas all three modifiers protect CALB from structural alterations during adsorption onto a hydrophilic support. Received: 18 March 1999 / Received revision: 21 June 1999 / Accepted: 27 June 1999     

Effect of the Immobilization Method of Lipase from Thermomyces lanuginosus on Sucrose Acylation

Lipase from Thermomyces lanuginosus (formerly Humicola lanuginosa ) was immobilized using granulation by incubating low-particle-size silica with the lipase. Granules with a particle diameter in the range 0.3-1 &#117 mm were obtained. The immobilized lipase was tested in the acylation of sucrose with vinyl laurate in mixtures of tert -amyl alcohol: dimethyl sulfoxide. Results were compared with immobilization of enzyme by adsorption on polypropylene (Accurel EP100), deposition on Celite by precipitation, and covalent attachment to Eupergit C. Granulated lipase converted >95% of sucrose into 6- O -lauroylsucrose in 6 &#117 h. Accurel-lipase was also very active, converting 70% of sucrose into monoester in 2 &#117 h. The residual activity of granules after five reaction cycles under the best reaction conditions was 72%; this value was considerably higher than the one observed for the same lipase adsorbed on Accurel (15% residual activity after five cycles).     

Immobilization of β-galactosidase from Kluyveromyces lactis on silica and agarose: comparison of different methods

The covalent immobilization of β-galactosidase from Kluyveromyces lactis (β-gal) on to two different porous carriers, CPC-silica and agarose, is reported. CPC-silica was silanizated and activated with glutaraldehyde. The activation of agarose via a cyanylating agent (CDAP) was optimized. Gel-bound protein and gel-bound activity were both measured directly, allowing the determination of apparent specific activities (S.A.). Higher amounts of β-gal were immobilized on the activated CPC-silica (maximum capacity, 23 mg ml⁻¹ of packed support) than on the CDAP-activated agarose. For the lower enzyme loading assayed (12.6 mg ml⁻¹ packed support), 100% of the enzyme was immobilized but only 34% of its activity was expressed. This inactivation during immobilization was confirmed by the S.A. values (22–29 EU mg⁻¹ for the CPC-derivatives and 80 EU mg⁻¹ for soluble β-gal). The K_app (3.4 mM) for the CDAP-derivative with ONPG as substrate was higher than the K_M value for soluble β-gal (2 mM). When the enzyme loading was increased five-fold, the K_app increased four-fold, to 13 mM. The V_app values for the CPC-derivatives were remarkably lower than the V_max for soluble β-galactosidase. CDAP-derivatives showed better thermal stabilities than CPC-derivatives but neither of them enhanced the stability of the soluble enzyme. When stored at 4°C, the activity of both derivatives remained stable for at least 2 months. Both derivatives displayed high percentages of lactose conversion (90%) in packed bed mini-reactors. Glucose production was 3.3-fold higher for the CPC-derivative than for the CDAP-derivative, as a consequence of the higher flow rates achieved.     

An efficient system for catalyzing ester synthesis using a lipase from a newly isolated Burkholderia cepacia strain

The synthesis of ethyl-oleate by the lipase from the newly isolated strain Burkholderia cepacia LTEB11 in three different systems has been studied – immobilization on a hydrophobic support (Accurel EP 100®), encapsulation in reverse micelles, and direct addition of powdered free enzyme to the reaction medium. The immobilized enzyme performed best, giving a 70% ester yield in 10 h, this yield being five-fold greater than that obtained for reversed micelles, and two and a half times greater than that obtained for direct addition. An increase in the amount of immobilized enzyme preparation added gave a 100% ester yield in 3 h. The immobilized preparation was quite stable, giving a 100% yield of ethyl-oleate during 11 repeated reactions, and 50% yield after 24 reactions. These results suggest that the lipase of our strain of B. cepacia LTEB11 immobilized on Accurel has good potential for application in biocatalysis in organic media.