Structure and conformational flexibility of Candida rugosa lipase

Anandamide, an endogenous ligand for cannabinoid receptors, loses its biological activities when it is hydrolyzed to arachidonic acid and ethanolamine by anandamide amidohydrolase. We overexpressed a recombinant rat enzyme with a hexahistidine tag in a baculovirus-insect cell expression system, and purified the enzyme with the aid of a Ni-charged resin to a specific activity as high as 5.7 micromol/min/mg protein. The purified recombinant enzyme catalyzed not only the hydrolysis of anandamide and palmitoylethanolamide, but also their reverse synthetic reactions. In order to attain an equilibrium of the anandamide hydrolysis and its reverse reaction within 10 min, we utilized a large amount of the purified enzyme. The equilibrium constant ([arachidonic acid][ethanolamine])/([anandamide][water]) was calculated as 4x10(-3) (37 degrees C, pH 9.0). These experimental results with a purified enzyme preparation quantitatively confirmed the reversibility of the enzyme reaction previously observed with crude enzyme preparations.     

A model for lipase production by Candida rugosa

A model adequately describing the lipase production by Candida rugosa has been developed, calibrated and validated using new experimental data. Process modelling has been done using CAMBIO software (Computer Aided Modelling of BIOprocesses), allowing to easy and interactively test various hypothesis and reaction schemes.Olive oil, oleic acid and glycerol has been used as substrates. The model satisfactorily describes the time evolution of biomass growth as well as lipase production in all cases. In particular diauxic behavior is successfully characterized.Model development process has helped in obtaining a 3-fold increase in lipase production when using oleic acid as substrate instead of the original olive oil used.List of Symbols Oil g/l Oil concentration - Fa g/l Fatty acids concentration - Gly g/l Glycerol concentration - Cr g/l Biomass (dry weight) - Lp U/ml Lipase - _p Oil hydrolysis rate - _gly Uptake rate on glycerol - _fa Uptake rate on fatty acids - _lp Increase rate of lipase - Y _ca Biomass/Fatty acids yield - Y _cg Biomass/Glycerol yield - Y _la Lipase/Fatty acids yield - k _l Specific growth rate on fatty acids - K _c Saturation constant - K _I Inhibition constant for lipase - k11 Specific growth rate on glycerol - k ₃ Oil hydrolysis parameter     

Two conformational states of Candida rugosa lipase.

The structure of Candida rugosa lipase in a new crystal form has been determined and refined at 2.1 A resolution. The lipase molecule was found in an inactive conformation, with the active site shielded from the solvent by a part of the polypeptide chain-the flap. Comparison of this structure with the previously determined "open" form of this lipase, in which the active site is accessible to the solvent and presumably the substrate, shows that the transition between these 2 states requires only movement of the flap. The backbone NH groups forming the putative oxyanion hole do not change position during this rearrangement, indicating that this feature is preformed in the inactive state. The 2 lipase conformations probably correspond to states at opposite ends of the pathway of interfacial activation. Quantitative analysis indicates a large increase of the hydrophobic surface in the vicinity of the active site. The flap undergoes a flexible rearrangement during which some of its secondary structure refolds. The interactions of the flap with the rest of the protein change from mostly hydrophobic in the inactive form to largely hydrophilic in the "open" conformation. Although the flap movement cannot be described as a rigid body motion, it has very definite hinge points at Glu 66 and at Pro 92. The rearrangement is accompanied by a cis-trans isomerization of this proline, which likely increases the energy required for the transition between the 2 states, and may play a role in the stabilization of the active conformation at the water/lipid interface. Carbohydrate attached at Asn 351 also provides stabilization for the open conformation of the flap.     

Immobilisation ofCandida cylindracea lipase on a new range of ceramic supports

Summary Lipase fromC. cylindracea was covalently immobilised to a number of surface-treated ceramic supports (3–10 mg. (g dry wt support)^–1). At room temperature, the immobilised lipase could convert R,S-citronellol and butyric acid to citronellyl butyrate at rates in the range 7–51 mol. (mg lipase.min)^–1. The lipase maintained 90–100% of its initial activity over a period of 150 days.     

Rapid purification of two lipase isoenzymes from Candida rugosa

Summary We describe a two-step method for the purification of two lipases (lipases A and B) from C. rugosa. The purification procedure includes Phenyl-Sepharose and Sephacryl HR 100 chromatographies. The enzymes obtained were pure according to criteria of specific activity and neutral sugar content.     

Thermal stability enhancement of Candida rugosa lipase using ionic liquids

The thermal stability of Candida rugosa (C. rugosa) lipase was investigated and compared in n-hexane, benzene, dibutyl-ether as well as [bmim]PF₆ and [omim]PF₆ ionic liquids and the effect of solvent polarity and water activity were evaluated. Deactivation of the enzyme followed a series-type kinetic model. First order deactivation rate constants and the ratios of specific activities were determined and the kinetics of deactivation were studied. Among the organic solvents, the best stability was observed in n-hexane with a half-life of 6.5 h at water activity of 0.51. In ionic liquids, however, even longer half lives were obtained, and the enzyme was stable in these solvents at 50°C. The highest half-life times were obtained in [bmim]PF₆ (12.3 h) and [omim]PF₆ (10.6 h). A direct correlation was found between solvent polarity and thermal stability since the higher the polarity of the solvent, the lower was the stability decrease at 50°C comparing to that at 30°C.     

Immobilization of lipase from Candida rugosa on a polymer support

Lipase from Candida rugosa was immobilized by adsorption onto a macroporous copolymer support. Under optimum conditions the maximum amount of protein bound was 15.4 mg/g and the immobilization efficiency was 62%. The kinetics of lipase binding to the selected polymer carrier was assessed by using a general model of topochemical reactions. The effect of temperature on adsorption was thoroughly investigated, as was the adsorption mechanism itself. Analysis of the proposed kinetic model and the specific kinetic parameters measured suggest that surface kinetics control the adsorption process. According to the activation energy (E _a) and the rate constant, k, the enzyme has rather a high affinity for the support's active sites. The immobilized enzyme was used to catalyse the hydrolysis of palm oil in a lecithin/isooctane reaction system, in which the enzyme's activity was 70% that of the free enzyme. Kinetic parameters such as maximum velocity (V _max) and the Michaelis constant (K _m) were determined for the free and the immobilized lipase. Following repeated use, the immobilized lipase retained 56% of its initial activity after the fifth hydrolysis cycle. Received: 3 April 1998 / Received revision: 28 July 1998 / Accepted: 29 July 1998     

Immobilization of Candida rugosa lipase on electrospun cellulose nanofiber membrane

A biocatalyst with high activity retention of lipase was fabricated by the covalent immobilization of Candida rugosa lipase on a cellulose nanofiber membrane. This nanofiber membrane was composed of nonwoven fibers with 200 nm nominal fiber diameter. It was prepared by electrospinning of cellulose acetate (CA) and then modified with alkaline hydrolysis to convert the nanofiber surface into regenerated cellulose (RC). The nanofiber membrane was further oxidized by NaIO₄. Aldehyde groups were simultaneously generated on the nanofiber surface for coupling with lipase. Response surface methodology (RSM) was applied to model and optimize the modification conditions, namely NaIO₄ content (2–10 mg/mL), reaction time (2–10 h), reaction temperature (25–35 °C) and reaction pH (5.5–6.5). Well-correlating models were established for the residual activity of the immobilized enzyme (R² = 0.9228 and 0.8950). We found an enzymatic activity of 29.6 U/g of the biocatalyst was obtained with optimum operational conditions. The immobilized lipase exhibited significantly higher thermal stability and durability than equivalent free enzyme.     

Thermal stability enhancement of Candida rugosa lipase using ionic liquids

The thermal stability of Candida rugosa (C. rugosa) lipase was investigated and compared in n-hexane, benzene, dibutyl-ether as well as [bmim]PF₆ and [omim]PF₆ ionic liquids and the effect of solvent polarity and water activity were evaluated. Deactivation of the enzyme followed a series-type kinetic model. First order deactivation rate constants and the ratios of specific activities were determined and the kinetics of deactivation were studied. Among the organic solvents, the best stability was observed in n-hexane with a half-life of 6.5?h at water activity of 0.51. In ionic liquids, however, even longer half lives were obtained, and the enzyme was stable in these solvents at 50°C. The highest half-life times were obtained in [bmim]PF₆ (12.3?h) and [omim]PF₆ (10.6?h). A direct correlation was found between solvent polarity and thermal stability since the higher the polarity of the solvent, the lower was the stability decrease at 50°C comparing to that at 30°C.     

Action of Candida rugosa lipase in carvone isomers as solvents

The activity and enantioselectivity of Candida rugosa lipase were investigated in chiral solvents, (–)-, (+)- and racemic carvone, for the resolution of 2-chloro-propionic acid with n-butanol via esterification. The activity of the enzyme studied was about 50% higher in (–)-carvone than in (+)-carvone, however the enantioselectivity was similar.     

Reaction scheme of lipase production byCandida rugosa growing on olive oil

Summary In a study of lipase production byCandida rugosa growing on olive oil, the relationship between the consumption of substrate and lipase production is presented. Two stages could be observed in the consumption of the olive oil: a first one, related with the glycerol depletion without lipase production, and a second one, associated with the fatty acids consumption when the enzyme appears in the medium.     

Effect of different carbon sources on lipase production by Candida rugosa

Different carbon sources affecting growth and lipase production in Candida rugosa were studied by using batch cultures on defined medium. Carbohydrates and acids non-related to fats did not induce lipase production. The highest yields of enzyme were obtained with lipids or fatty acids as carbon sources. Tween 80 stimulated lipase biosynthesis and secretion outside the cell. Combinations of two types of substrates, carbohydrates and fatty acids, did not improve lipase production, and in some cases, their consumption was produced in a sequential pattern. Glucose presented a repressing effect on lipase production. Moreover, glucose was found to be effective in stimulating lipase secretion by cells with a high level of cell-bound lipase activity because of their previous growth in oleic acid.     

Active biocatalysts based on Candida rugosa lipase immobilized in vesicular silica

Vesicular silica (VS) with hierarchical structure was prepared by utilizing cationic surfactant cetyltrimethylammonium bromide (CTAB) and anionic surfactant sodium dodecyl sulfate (SDS) as the structure directing agents, and 1,3,5-triisopropylbenzene (TIPB) as the micelle expander. The resulting unilamellar and multilamellar VS with interlamellar mean mesopore size of 15–20 nm and shell thickness of 5–15 nm were used as supports for immobilization of Candida rugosa lipase (CRL) through physical adsorption. Possible mechanisms for the formation of VS and the immobilization of CRL on VS are proposed. N₂ adsorption-desorption experiments and Fourier transform infrared spectroscopy (FT-IR) measurements demonstrated that CRL was adsorbed into the curved channels of the VS. The catalytic activity, thermal stability, and reusability of VS immobilized CRL were assayed in phosphate buffer medium by hydrolysis of triacetin. The effects of pH and temperature on enzyme activity were also investigated. We report that VS immobilized CRL exhibited outstanding adaptability at higher pH and temperature, and excellent thermal stability and reusability compared with free CRL.     

New differences between isoenzymes A and B from Candida rugosa lipase

Water adsorption isotherms of pure lipases A and B from Candida rugosa are different and can be used to distinguish between the isoenzymes. The maximum esterification yield (50%, 20h) can be achieved at initial 0.9<1.0. Lipase B is more stereoselective (49% yield, 98% enantiomeri excess) than lipase A (47% yield, 72% enantiomerci excess) but both isoenzymes mainly esterify the (S) 2(4-isobutylphenyl)propionic acid (Ibuprofen).     

Effects of different fatty acids in lipase production by Candida rugosa

Summary Oleic acid has been reported as a good inducer of lipase production by Candida rugosa. In order to know if this enzyme is induced by oleic acid itself or by a metabolite, different short chain fatty acids were tested. Butyric acid was the best carbon source to growth microorganism but it did not induce lipase production. Although caprylic and capric acid were the best inducers of lipase production, at concentrations up 1 g/l they have toxic effect in Candida rugosa growth. Thus, from the point of view of industrial production oleic acid could be considered as the best substrate tested.     

Enhanced activity of Candida rugosa lipase modified by polyethylene glycol derivatives

The derivatives of polyethylene glycol (PEG) were prepared by reacting PEG with propylene oxide to enhance its hydrophobicity and introduce a branched structure. The PEG derivatives were activated with cyanuric chloride and used to modify the lipase fromCandida rugosa. The maximum specific activity of lipase modified with the PEG derivatives was about 2-fold of that modified with PEG for the esterification of oleic acid and lauryl alcohol in hexane.     

Purification and characterization of two isoforms from Candida rugosa lipase B

Two isoforms of Candida rugosalipase B (LB1 and LB2) were purified by anionic exchange chromatography. The lipases had the same N-terminal sequence, carbohydrate content and pH and thermal stability but different pIs and significant differences in their activities against different p-nitrophenol esters and triacylglycerides.     

Polymerization of propyl malolactonate in the presence of Candida rugosa lipase

To gain better insight into mechanistic features of enzyme-catalyzed malolactonate polymerization, reactions with propyl malolactonate were analyzed while varying enzyme concentration, reaction media composition, and reaction temperature. Monomer conversion and product molecular weights were characterized by (1)H NMR and MALDI-TOF MS, respectively. A high extent of thermal polymerization of propyl malolactonate was observed, while the polymer chain length in all reactions was controlled by the elimination of alpha-hydrogen from propyl malolactonate with formation of a new initiator and the new chains. The most efficient enzymatic catalysis occurred in toluene (2.11 M monomer) at 60 degrees C. Candida rugosa lipase (10 wt %) accelerated polymerization 25-fold over the rate of thermal polymerization. The maximum poly(propyl malate) number-average molecular weight obtained was 5000 Da at 20 wt % enzyme with a polydispersity of 1.15. These values compare with 1800 Da and 1.5, respectively, in the absence of enzyme.     

Strategies for the production of lipase by Candida rugosa; neural estimation of biomass and lipase activity

Summary Various strategies for the production of lipase by Candida rugosa Diddens and Lodder (ATCC 14830) in stirred tank reactors were investigated. The strain was first screened for lipase production with agar plate assay based on the fluorescent dye Rhodamine B, followed by adaptation to the production medium used. The highest lipase activity of 7.6 U/ml was obtained on a medium containing 40 g olive oil/l and 1 g glucose/l, with supplying pure oxygen. Neural networks were used in the estimation of biomass and lipase activity.