Covalent immobilization of lipase from Candida rugosa onto poly(acrylonitrile-co-2-hydroxyethyl methacrylate) electrospun fibrous membranes for potential bioreactor application

A simple way of fabricating enzymatic membrane reactor with high enzyme loading and activity retention from the conjugation between nanofibrous membrane and lipase was devised. Poly(acrylonitrile-co-2-hydroxyethyl methacrylate) (PANCHEMA) was electrospun into fibrous membrane and used as support for enzyme immobilization. The hydroxyl groups on the fibrous membrane surface were activated with epichlorohydrin, cyanuric chloride or p-benzoquinone, respectively. Lipase from Candida rugosa was covalently immobilized on these fibrous membranes. The resulted bioactive fibrous membranes were examined in catalytic efficiency and activity for hydrolysis. The observed enzyme loading on the fibrous membrane with fiber diameter of 80–150 nm was up to 1.6% (wt/wt), which was as thrice as that on the fibrous membrane with fiber diameter of 800–1000 nm. Activity retention for the immobilized lipase varied between 32.5% and 40.6% with the activation methods of hydroxyl groups. Stabilities of the immobilized lipase were obviously improved. In addition, continuous hydrolysis was carried out with an enzyme-immobilized fibrous membrane bioreactor and a steady hydrolysis conversion (3.6%) was obtained at a 0.23 mL/min flow rate under optimum condition.     

Development and intracellular localization of lipase activity in rapessed (Brassica napus L.) cotyledons

In homogenates of resting rapeseeds no lipase activity (glycerolester hydrolase, EC 3.1.1.3) could be detected using a titrimetric assay procedure. Following a 30-h lag-phase after imbibition, lipase activity increased sharply, reaching its maximum at day 4 after sowing. Simultaneously triglyceride content of the cotyledons decreased sharply. At any time during the 11-day period of seedling growth examined, only an alkaline lipase activity with a pH optimum around 9 was present. White light had essentially no effect on the development of lipase activity. However, the disappearance of lipase activity from the cotyledons after fat utilization was found to depend on nitrogen nutrition of the seedlings. The activities of the glyoxysomal enzymes catalase and malate synthetase showed the usual rise and fall patterns with peak activities at day 4 after sowing, independently of the mineral nutrition of the seedlings.About 90% of the lipase activity was associated with a microsomal membrane fraction. Resolution of this fraction by sucrose density gradient centrifugation (62,000 g for 14 h) yielded three distinct membrane fractions. Maximum activities of membrane marker enzymes were recovered from the gradients at following densities: The major portion of microsomal protein and lipase activity at 1.085 kg/l; microsomal malate synthetase and phosphorylcholineglyceride transferase at 1.116 kg/l; NADH-cytochrome c reductase and phosphorylcholinecytidyl transferase at 1.133 kg/l. Evidently in rapeseed cotyledons lipase activity is associated only with a discrete microsomal membrane fraction which sediments differently from membrane fractions of the endoplasmic reticulum.     

Use of stable emulsion to improve stability, activity, and enantioselectivity of lipase immobilized in a membrane reactor

The enantiocatalytic performance of immobilized lipase in an emulsion membrane reactor using stable emulsion prepared by membrane emulsification technology was studied. The production of optical pure (S)-naproxen from racemic naproxen methyl ester was used as a model reaction system. The O/W emulsion, containing the substrate in the organic phase, was fed to the enzyme membrane reactor from shell-to-lumen. The enzyme was immobilized in the sponge layer (shell side) of capillary polyamide membrane with 50 kDa cut-off. The aqueous phase was able to permeate through the membrane while the microemulsion was retained by the thin selective layer. Therefore, the substrate was kept in the enzyme-loaded membrane while the water-soluble product was continuously removed from the reaction site. The results show that lipase maintained stable activity during the entire operation time (more than 250 h), showing an enantiomeric excess (96 +/- 2%) comparable to the free enzyme (98 +/- 1%) and much higher compared to similar lipase-loaded membrane reactors used in two-separate phase systems (90%). The results demonstrate that immobilized enzymes can achieve high stability as well as high catalytic activity and enantioselectivity.     

Characterization of a Triacylglycerol Lipase That Liberates Arachidonic Acid from Bovine Chromaffin Cells During Secretion

Abstract: Primary cultures of chromaffin cells from bovine adrenal medullae were used as a model to study lipolytic events during stimulus-secretion coupling. It has been shown that chromaffin cells liberate arachidonic acid in addition to their main secretion product, the catecholamines. To understand more about the mechanism of arachidonic acid liberation, chromaffin cells were labeled with radioactive arachidonic acid, stimulated, and then analyzed for changes in lipid composition. After stimulation with 10^?4M acetylcholine, the radioactivity of triacylglycerols decreased to the same extent that the free arachidonic acid level rose. This finding suggests that in bovine chromaffin cells a stimulation-dependent triacylglycerol lipase (triacylglycerol hydrolase; EC 3.1.1.3) is involved in arachidonic acid liberation. Further work was performed on detection, characterization, and isolation of this enzyme. Triacylglycerol lipase activity was found in whole cell homogenates and in plasma membrane fractions isolated from adrenal medullary tissue. The plasma membrane lipase showed a pH optimum of 4.3. The apparent Michaelis constant was determined as 3.3 × 10^?4 mol/L. Ca²⁺ did not influence the enzymatic activity. To differentiate the plasma membrane triacylglycerol lipase from the previously described plasma membrane diacylglycerol lipase of chromaffin cells, the influence of RG 80267, a specific diacylglycerol lipase inhibitor, was examined. RG 80267 (50 μM) inhibited the triacylglycerol lipase by only 24%, although diacylglycerol lipase was totally inhibited with only 20 μM RG 80267. The pH optimum of homogenate lipase was broad, lying between 4 and 7. Starting from the soluble fraction of whole cell homogenates, the triacylglycerol lipase was partially purified by ultracentrifugation and size-exclusion chromatography. The molecular mass of the enzyme as determined by sodium dodecyl sulfate-polyacrylamide gel electrophoresis was found to be between 47 and 57 kDa.     

Membrane microreactor in biocatalytic transesterification of triolein for biodiesel production

Transesterification is a principal chemical reaction that occurs in biodiesel production. We developed a novel biocatalytic membrane microreactor (BMM) for continuous transesterification by utilizing an asymmetric membrane as an enzyme-carrier for immobilization. The BMM was developed by pressure driven filtration of lipase from Pseudomonas fluorescens, which is suitable for highly efficient biocatalytic transesterification. Lipase solution was allowed to permeate through an asymmetric membrane with NMWL 300 kDa composed of polyethersulfone. The performances of BMM were studied in biodiesel synthesis via transesterification of triolein with methanol. Transesterification was carried out by passing a solution of triolein and methanol through the asymmetric membrane. The degree of triolein conversion using this microreactor was ca. 80% with a reaction time of 19 min. The BMM system displayed good stability, with no activity decay over a period of 12 day with continuous operation. Results from triolein transesterification clearly demonstrate the potential of an asymmetric membrane as an enzyme carrier material. Enzyme activity (mmol/h·g_lipase) was approximately 3 fold higher than that of native free lipase.     

Enantioselective esterification of butanol-2 in an enzyme membrane reactor

The enzymatic esterification of octanoic acid with racemic butanol-2 was investigated. Esterifications of the acid were performed in a forced flow enzyme membrane reactor. The used membrane was prepared by a phase inversion process in polyamide-6 solution followed by the chemical immobilization of a lipase-catalyst. Influences of water content and pH were estimated. Their optimum values are equal to 0.5% w/w and pH 8. The reaction rate (at 303 K) of 5.1 × 10^?5 mol/h·cm² of the membrane area, and at least 85% enantiomeric excess in the produced ester mixture were obtained. The activity of immobilized lipase in the membrane process is about two times higher than that of the native lipase in the esterification performed in a tank reactor.     

Lipase catalyzed methanolysis to produce biodiesel: Optimization of the biodiesel production

A lipase from Candida sp., suitable for transesterification of fats and oils to produce fatty acid methyl ester (FAME), was immobilized on a cheap cotton membrane, in this paper. The conversion ratio of salad oil to biodiesel could reach up to 96% with the optimal reaction conditions. Continuous reaction in a fixed bed reactor was also investigated. A three-step transesterification with methanol (methanolysis) of oil was conducted by using a series of nine columns packed with immobilized Candida sp. 99–125 lipase. As substrate of the first reaction step, plant or waste oil was used together with 1/3 molar equivalent of methanol against total fatty acids in the oil. Mixtures of the first- and second-step eluates and 1/3 molar equivalent of methanol were used for the second- and third-reaction steps. A hydrocyclone was used in order to on-line separate the by-product glycerol after every 1/3 molar equivalent of methanol was added. Petroleum ether was used as solvent (3/2, v/v of oil) and the pump was operated with a flow rate of 15 L/h giving an annual throughput of 100 t. The final conversion ratio of the FAME from plant oil and waste oil under the optimal condition was 90% and 92%, respectively. The life of the immobilized lipase was more than 10 days. This new technique has many strongpoints such as low pollution, environmentally friendly, and low energy costs.     

Hydrolysis of olive oil catalyzed by surfactant-coated<Emphasis Type="Italic">Candida rugosa</Emphasis> lipase in a hollow fiber membrane reactor

In this study, we invetigated the hydrolysis of olive oil catalyzed by a surfactant-coatedCandida rugosa lipase in a hydrophilic polyacrylonitrile hollow fiber membrane reactor and then compared the results to those using the native lipase. The organic phase was passed through the hollow inner fibers of the reactor and consisted of either the coated lipase and olive oil dissolved in isooctane or the coated lipase dissolved in pure olive oil. The aqueous phase was pumped through the outer space. After 12 h and with conditions of 30°C, 0.12 mg enzyme/mL and 0.62 M olive oil, the substrate conversion of the coated lipase reached 60%. This was twice the conversion for the same amount of native lipase that was pre-immobilized on the membrane surface. When using pure olive oil, after 12 h the substrate conversion of the coated lipase was 50%. which was 1.4 times higher than that of the native lipase.     

Mixed reverse micelles facilitated downstream processing of lipase involving water‐oil‐water liquid emulsion membrane

Our earlier work for the first time demonstrated that liquid emulsion membrane (LEM) containing reverse micelles could be successfully used for the downstream processing of lipase from Aspergillus niger. In the present work, we have attempted to increase the extraction and purification fold of lipase by using mixed reverse micelles (MRM) consisting of cationic and nonionic surfactants in LEM. It was basically prepared by addition of the internal aqueous phase solution to the organic phase followed by the redispersion of the emulsion in the feed phase containing enzyme, which resulted in globules of water‐oil‐water (WOW) emulsion for the extraction of lipase. The optimum conditions for maximum lipase recovery (100%) and purification fold (17.0‐fold) were CTAB concentration 0.075 M, Tween 80 concentration 0.012 M, at stirring speed of 500 rpm, contact time 15 min, internal aqueous phase pH 7, feed pH 9, KCl concentration 1 M, NaCl concentration 0.1 M, and ratio of membrane emulsion to feed volume 1:1. Incorporation of the nonionic surfactant (e.g., Tween 80) resulted in remarkable improvement in the purification fold (3.1–17.0) of the lipase. LEM containing a mixture of nonionic and cationic surfactants can be successfully used for the enhancement in the activity recovery and purification fold during downstream processing of enzymes/proteins. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1084–1092, 2014     

Phospholipase C and diacylglycerol lipase activities associated with plasma membranes of chromaffin cells isolated from bovine adrenal medulla

The plasma membranes of bovine adrenal chromaffin cells were isolated and the activities of enzymes involved in arachidonic acid liberation were investigated. Only a minute activity of phospholipase A2 (phosphatide 2-acylhydrolase, EC 3.1.1.4) could be detected using externally added phosphatidylcholine (PC) and phosphatidylethanolamine (PE) as substrate. When membranes were treated with exogenous phospholipase C (orthophosphoric acid diester phosphohydrolase, EC 3.1.4.1) there was a liberation of free fatty acids from the sn-2 position of PC. The enzyme responsible for this effect could be demonstrated to be a diacylglycerol lipase (glycerol ester hydrolase, EC 3.1.1.3) localized in the plasma membrane. Using phosphatidylinositol (PI) as a substrate, it was found that an endogenous phospholipase C exists which co-purifies with the membrane preparation. The produced diacylglycerol is subsequently hydrolyzed by diacylglycerol lipase liberating arachidonic acid. The two enzymes, phospholipase C and diacylglycerol lipase were characterized. Phospholipase C was found to be calcium dependent and PI specific, showing an activity of 60 pmol/micrograms protein per h (1.2 mM Ca2+), whereas the diacylglycerol lipase was calcium independent hydrolyzing diacylglycerol at a rate of 7.2 pmol/micrograms protein per h. The lipase but not the phospholipase C was inhibited 50% by 1.7 mM para-bromophenacylbromide.     

Display of Bacterial Lipase on the Escherichia coli Cell Surface by Using FadL as an Anchoring Motif and Use of the Enzyme in Enantioselective Biocatalysis

We have developed a novel cell surface display system by employing FadL as an anchoring motif, which is an outer membrane protein involved in long-chain fatty acid transport in Escherichia coli. A thermostable Bacillus sp. strain TG43 lipase (44.5 kDa) could be successfully displayed on the cell surface of E. coli in an active form by C-terminal deletion-fusion of lipase at the ninth external loop of FadL. The localization of the truncated FadL-lipase fusion protein on the cell surface was confirmed by confocal microscopy and Western blot analysis. Lipase activity was mainly detected with whole cells, but not with the culture supernatant, suggesting that cell lysis was not a problem. The activity of cell surface-displayed lipase was examined at different temperatures and pHs and was found to be the highest at 50°C and pH 9 to 10. Cell surface-displayed lipase was quite stable, even at 60 and 70°C, and retained over 90% of the full activity after incubation at 50°C for a week. As a potential application, cell surface-displayed lipase was used as a whole-cell catalyst for kinetic resolution of racemic methyl mandelate. In 36 h of reaction, (S)-mandelic acid could be produced with the enantiomeric excess of 99% and the enantiomeric ratio of 292, which are remarkably higher than values obtained with crude lipase or cross-linked lipase crystal. These results suggest that FadL may be a useful anchoring motif for displaying enzymes on the cell surface of E. coli for whole-cell biocatalysis.     

费希尔曲霉脂肪酶在毕赤酵母中的优化表达及高密度发酵

【背景】脂肪酶广泛应用于纺织、食品、药品、皮革等工业领域,其在微生物中的异源表达研究进一步促进了脂肪酶产品的生产和应用。【目的】实现来源于费希尔曲霉的脂肪酶在毕赤酵母中的高效异源表达,探究其合适的表达及发酵条件,提高产量,降低成本。【方法】对费希尔曲霉的脂肪酶编码基因进行密码子优化后,应用pPIC9k质粒整合到毕赤酵母GS115基因组上,构建高产脂肪酶Lip605的毕赤酵母工程菌;并通过响应面发酵条件优化、筛选最适伴侣蛋白和高密度发酵相结合的方法,综合提高脂肪酶表达量。【结果】确定高产脂肪酶毕赤酵母工程菌的最优摇瓶发酵产酶条件为:甲醇3.103%(体积比),生物素0.4 mg/L,酵母粉11.5 g/L,酵母基础氮源培养基(yeast nitrogen base,YNB) 13.4 g/L,初始pH 6.4,装液量50 mL/250 mL,转速220 r/min,温度24°C,培养时间40 h。优化后的胞外脂肪酶酶活达到72.34 U/mL,较优化前提高了5.8倍;进一步选择12个伴侣蛋白分别与脂肪酶Lip605进行共表达,其中共表达伴侣蛋白Rpl10(pPICZA-RPL10)效果最佳,可使Lip605表达量进一步提高46.8%;在此基础上,经过10 L发酵罐分批补料的高密度发酵,工程菌株发酵142 h,胞外脂肪酶酶活最高达到680 U/mL,蛋白浓度为15.89 g/L。【结论】应用复合策略有效提高了脂肪酶Lip605在毕赤酵母中的发酵产量,为其进一步工业化生产奠定了良好的基础。     

溶胶凝胶法固定化黑曲霉脂肪酶的性质研究

近年来溶胶-凝胶法固定脂肪酶已成为研究热点。选用TMOS、MTMS、ETMS和PTMS 4种硅烷试剂对黑曲霉脂肪酶进行了固定化研究。固定化的最佳配方为ETMS/TMOS=5：1、水与硅烷试剂分子比为8;固定化脂肪酶的固定率为80.2%、相对活性为136.3%;以乳化橄榄油作为底物,在50℃和pH4.0的条件下,固定化脂肪酶与游离脂肪酶K_m分别为1.899×10^-4M和2.789×10^-4M;最适反应pH均为pH4.0,固定化脂肪酶在pH4.0~pH5.5之间其活性能保持95%以上;固定化脂肪酶最适反应温度为60℃,较游离脂肪酶提高了10℃;固定化脂肪酶的酸碱稳定性和热稳定性较非固定化酶有显著的提高。固定化脂肪酶的使用寿命和保存稳定性良好,使用12次后仍能够保留71.7%活性,在室温避光条件下保存180天后仍可保留79.2%活性。     

Expression of a lipase on the cell-surface of Escherichia coli using the OmpW anchoring motif and its application to enantioselective reactions

Microbial-surface display is the expression of proteins or peptides on the surface of cells by fusing an appropriate protein as an anchoring motif. Here, the outer membrane protein W (OmpW) was selected as a fusion partner for functional expression of Pseudomonas fluorescence SIK W1 lipase (TliA) on the cell-surface of Escherichia coli. Localization of the truncated OmpW-TliA fusion protein on the cell-surface was confirmed by immunoblotting and functional assay of lipase activity. Enantioselective hydrolysis of rac-phenylethyl butanoate by the displayed lipase resulted in optically active (R)-phenyl ethanol with 96 % enantiomeric excess and 44 % of conversion in 5 days. Thus, a small outer membrane protein OmpW, is a useful anchoring motif for displaying an active enzyme of ~50 kDa on the cell-surface and the surface-displayed lipase can be employed as an enantioselective biocatalyst in organic synthesis.     

Display of bacterial lipase on the Escherichia coli cell surface by using FadL as an anchoring motif and use of the enzyme in enantioselective biocatalysis

We have developed a novel cell surface display system by employing FadL as an anchoring motif, which is an outer membrane protein involved in long-chain fatty acid transport in Escherichia coli. A thermostable Bacillus sp. strain TG43 lipase (44.5 kDa) could be successfully displayed on the cell surface of E. coli in an active form by C-terminal deletion-fusion of lipase at the ninth external loop of FadL. The localization of the truncated FadL-lipase fusion protein on the cell surface was confirmed by confocal microscopy and Western blot analysis. Lipase activity was mainly detected with whole cells, but not with the culture supernatant, suggesting that cell lysis was not a problem. The activity of cell surface-displayed lipase was examined at different temperatures and pHs and was found to be the highest at 50 degrees C and pH 9 to 10. Cell surface-displayed lipase was quite stable, even at 60 and 70 degrees C, and retained over 90% of the full activity after incubation at 50 degrees C for a week. As a potential application, cell surface-displayed lipase was used as a whole-cell catalyst for kinetic resolution of racemic methyl mandelate. In 36 h of reaction, (S)-mandelic acid could be produced with the enantiomeric excess of 99% and the enantiomeric ratio of 292, which are remarkably higher than values obtained with crude lipase or cross-linked lipase crystal. These results suggest that FadL may be a useful anchoring motif for displaying enzymes on the cell surface of E. coli for whole-cell biocatalysis.     

High-level expression of extracellular lipase Lip2 from Yarrowia lipolytica in Pichia pastoris and its purification and characterization

The extracellular lipase gene from Yarrowia lipolytica (YlLip2) was cloned into the pPICZalphaA and integrated into the genome of the methylotrophic yeast Pichia pastoris X-33. The lipase was successfully expressed and secreted with an apparent molecular weight of 39kDa using Saccharomyces cerevisiae secretion signal peptide (alpha-factor) under the control of the methanol inducible promoter of the alcohol oxidase 1 gene (AOX1). The lipase activity of 12,500,000U/l (2.10g total protein and 0.63g lipase per liter) was obtained in a fed-batch cultivation, where methanol feeding was linked to the dissolved oxygen content after initial glycerol culture. After fermentation, the supernatant was concentrated by ultrafiltration with a 10kDa cut off membrane and purified with ion exchange chromatography using Q Sepharose FF. Deglycosylation showed that the recombinant lipase is a glycoprotein which contains the same content of sugar (about 12%) as the native lipase from Y. lipolytica. The optimum temperature and pH of the recombinant lipase was 40 degrees C and 8.0, respectively. The lipase showed high activity toward long-chain fatty acid methyl esters (C12-C16).     

The action of phospholipase C and lipase on black film bilayer membranes

Phospholipase C(C. perfringens) added to one side of a phosphatidyl choline—phosphatidyl serine—cholesterol (0.7: 0.3: 1.0, w/w/w) bilayer membrane resulted in a rapid decrease in membrane resistance which leveled off after several minutes at about one-half its initial value. Pancreatic lipase added at this time resulted in a rapid increase in membrane resistance to a value somewhat higher than the initial. This effect was independent of the side to which the lipase was added, indicating that diglyceride is rapidly equilibrated across both sides of the membrane. When both phospholipase C and lipase were added at zero time to the same or opposite sides, the resistance decreased slightly and then increased to a value higher than the initial. Replacement of phosphatidyl choline by 2-hexadecoxy-3-octadecoxypropyl-phosphonylcholine, a phosphonate analog, resulted in an inhibition of the phospholipase C reaction which was equal to the percent analog. The analog, thus, seemed to act only as inert lipid and did not inhibit hydrolys of the active lipid.     

Exploring the effects of oil inducer on whole cell-mediated methanolysis for biodiesel production

Whole cell-mediated methanolysis of renewable oils for biodiesel production has drawn much attention in recent years since it can avoid the complex preparation procedures of traditional immobilized lipase. During the cultivation of Rhizopus oryzae whole cell catalyst, plant oils are usually added into the medium as inducer for lipase synthesis. It was found that oil inducer not only influenced lipase production, but also led to varied whole cell's catalytic performance. In this paper, the related mechanisms were explored and it was found that the higher unsaturated fatty acid (UFA) was contained in oil inducer, the higher intracellular lipase could be obtained. Different oil inducers also resulted in varied compositions of cell membrane, which was further found to be responsible for the operational stability of the catalyst. Cells with membrane enriched with saturated fatty acid (SFA) exhibited better stability than those enriched with UFA. And further study showed that after glutaraldehyde cross-linking treatment, the operational stability of both UFA enriched cells and SFA enriched cells were enhanced greatly and no loss in cell's catalytic activity was detected after being repeatedly used for 15 batches.     

Influence of ionic liquids as additives on sol–gel immobilized lipase

The immobilization of lipase from Candida rugosa, using ionic liquids as additives to protect the inactivation of lipase by released alcohol and shrinking of gel during sol–gel process, was investigated. The influence of various factors, such as structure of ionic liquids, content of ionic liquids and types of precursor in the sol–gel process on the activity and stability of immobilized lipase was also studied. The highest hydrolytic activity of immobilized lipase was obtained when the hydrophilic ionic liquid, [C₂mim][BF₄], was used as an additive, while the highest stability of immobilized lipase was obtained by using hydrophobic ionic liquid, [C₁₆mim][Tf₂N]. Therefore, the binary mixtures of these ionic liquids as additives were used to obtain the optimal immobilized lipase, which shows both high activity and stability. The hydrolysis and esterification activities of lipase co-immobilized with the mixture of 1:1 at molar ratio of [C₂mim][BF₄] and [C₁₆mim][Tf₂N] were 10-fold and 14-fold greater than in silica gel without ionic liquids (ILs), respectively. After 5 days incubation of this immobilized lipase in n-hexane at 50 °C, 84% of initial activity was remained, while the residual activity of the lipase immobilized without ILs was 28%.     

Optimization of culture conditions and properties of lipase from Penicillium camembertii Thom PG-3

The culture medium including nitrogen source, carbon source and metal ions, for lipase from Penicillium camembertii Thom PG-3 was optimized and the optimal medium consisted of soybean meal (fat free) 4%, Jojoba oil 0.5%, (NH₄)₂HPO₄, 0.1% Tween 60, initial pH 6.4 and the inoculation was at 28 °C for 96 h. The lipase activity produced was enhanced 3.9-fold and reached 500 U/ml. The lipase was purified 19.8-fold by pH precipitation, ethanol precipitation and ammonium sulphate precipitation as well as DEAE-cellulose chromatography. The purified lipase showed one polypeptide band in SDS-polyacrylamide gel electrophoreses (SDS-PAGE) with molecular weight 28.18 kDa. The optimal pH and temperature for activity of lipase were 6.4 and 48 °C, respectively, which are higher than those lipases from other penicillium sources. The P. camembertii Thom lipase is 1,3-positional specificity for hydrolysis of triglyceride and hydrolyses plant oil preferentially to animal oil. The lipase can be used in short chain ester synthesis with an esterification degree of 95%.