Enzymic interesterification of fats: The effect of non-lipase material on immobilized enzyme activity

An immobilized lipase (triacylglycerol acylhydrolase, EC 3.1.1.3) suitable for fat interesterification has been prepared by precipitation onto diatomaceous earth (Celite) with acetone of a crude lipase preparation from an Aspergillus. Non-lipase material present in the preparation which precipitated at high acetone concentrations or ovalbumin added prior to the immobilization reduced the measured interesterification activity without affecting lipolytic activity. The non-lipase material reduced the interesterification activity by as much as 50%. The interesterification activity of immobilized preparations was enhanced by the use of higher concentrations of the crude lipase or, more substantially, by admixture of purified lipase.     

Unexpected reaction profile observed in the synthesis of propyl laurate when using Candida rugosa lipases immobilized in microemulsions based organogels

1-Propyl laurate synthesis should not be used as standard reaction test of immobilized enzymes in microemulsion-based organogels (MBGs) prepared using lecithin/1-propanol as surfactant when extremely active enzymes with high load are used. In these cases, an anomalous kinetic reaction constant value is observed over short reaction times. Such an anomalous profile is strongly dependent on the concentration of catalyst in the crude powder and, consequently, is not appreciated when either commercial or low activity lipase samples are employed.     

Unexpected reaction profile observed in the synthesis of propyl laurate when using Candida rugosa lipases immobilized in microemulsions based organogels

1-Propyl laurate synthesis should not be used as standard reaction test of immobilized enzymes in microemulsion-based organogels (MBGs) prepared using lecithin/1-propanol as surfactant when extremely active enzymes with high load are used. In these cases, an anomalous kinetic reaction constant value is observed over short reaction times. Such an anomalous profile is strongly dependent on the concentration of catalyst in the crude powder and, consequently, is not appreciated when either commercial or low activity lipase samples are employed.     

A novel support for the immobilization of lipase and the effects of the details of its preparation on the hydrolysis of triacylglycerides

Summary The lipase from Candida cylindracea was immobilized by its adsorption on the internal surface of hydrophobic microporous poly(styrene-divinylbenzene) supports prepared by the concentrated emulsion polymerization method. The prepared supports have a surface area of the order of 200 m²/g. The immobilized enzyme catalyst is used for the hydrolysis of triacylglycerides. The effects of the amounts of surfactant and divinylbenzene used in the preparation of the hydrophobic support on the adsorption capacity for lipase and on the activity of the immobilized lipase have been investigated. The activity of the immobilized enzyme per enzyme molecule can be higher than that of the free lipase.     

Fatty-acid-modified enzymes as enantioselective catalysts in microaqueous organic media

Highly active lipase and protease complexes were prepared by non-covalent modification with stearic acid. The protein content and yield of the modified enzyme complexes depended on the enzymes' source. The increase in the transesterification activity of the modified enzymes was 15 fold for Candida rugosa lipase and porcine pancreatic lipase, with preservation of the enantioselectivity. Pseudomonas sp. lipase which showed no activity in its crude form, exhibited an activity of 38 mol/h·mg protein in the modified form. © Rapid Science Ltd. 1998     

A colorimetric microplate assay method for high throughput analysis of lipase activity

The present work describes a colorimetric microplate assay for lipase activity based on the reaction between 5,5'-dithiobis(2-nitro benzoic acid) (DTNB) and the hydrolysis product of 2,3-dimercapto-1-propanol tributyrate (DMPTB). Reaction mixtures containing DTNB, DMPTB, and lipase were prepared in microplate wells, and the absorbance at 405nm was recorded after incubation at 37 degrees C for 30 min. A linear relationship was obtained in the range of 0.1-1 U of lipase activity by this method. The reaction conditions were also optimized for the range of 0.01-0.1 U or 1-10 U. When assaying crude tissue extracts, the reaction of DTNB with non-specific reducing agents created a major source of error. However, this error was corrected by the use of blank samples that did not contain DMPTB.     

Hyperactivation of Rhizomucor miehei lipase by hydrophobic xerogels

Although a variety of approaches exist for the immobilization of enzymes, the "science" of enzyme immobilization is still in its infancy. In recent years, considerable interest has developed regarding the use of xerogels for enzyme immobilization. There are several advantages to xerogels for enzyme immobilization, including the opportunity to produce them in defined shapes or thin films and the ability to manipulate their physical characteristics (e.g., porosity, hydrophobicity, and optical properties). In this study we examined the effect of xerogel hydrophobicity on the activity of lipase (EC 3.2.2.3) from Rhizomucor miehei. The hydrophobicity of the xerogels was manipulated by generating xerogels with various molar ratios of propyltrimethoxysilane (PTMS) to tetramethoxysilane (TMOS), from 1:1 to 10:1. The belief was that, by increasing the proportion of propyl groups, the hydrophobicity of the resulting xerogel would be increased. Differences in the hydrophobicity of the resulting xerogels were confirmed using water-affinity studies. Two approaches were taken for water-affinity determinations by examining the ability of the xerogels to remove water from air (controlled humidity) and from water-saturated isopropyl ether. Xerogels with higher propyl content showed a reduced affinity for water. A crude lipase preparation from Rhizomucor miehei was then contacted with sized xerogel particulates and the effect of the xerogel on lipase activity was determined. The presence of the xerogel resulted in hyperactivation of the lipase. Analysis of the protein adsorption revealed changes in the profile of proteins adsorbed to the xerogel based on the hydrophobicity of the xerogel. Based on estimations of the specific activity of the hyperactivated lipase, a minimum hyperactivation of 207% was observed. Part of the hyperactivation may be attributable to xerogel-lipase interactions, but also to the adsorption of a component from the crude lipase preparation that may complex with the lipase and the xerogel producing a stabilizing effect. Further improvements in hyperactivation and selectivity of the xerogels is likely possible by working at lower PTMS:TMOS ratios than those investigated in this study.     

Lipase-mediated conversion of vegetable oils into biodiesel using ethyl acetate as acyl acceptor

Ethyl acetate was explored as an acyl acceptor for immobilized lipase-catalyzed preparation of biodiesel from the crude oils of Jatropha curcas (jatropha), Pongamia pinnata (karanj) and Helianthus annuus (sunflower). The optimum reaction conditions for interesterification of the oils with ethyl acetate were 10% of Novozym-435 (immobilized Candida antarctica lipase B) based on oil weight, ethyl acetate to oil molar ratio of 11:1 and the reaction period of 12h at 50 degrees C. The maximum yield of ethyl esters was 91.3%, 90% and 92.7% with crude jatropha, karanj and sunflower oils, respectively under the above optimum conditions. Reusability of the lipase over repeated cycles in interesterification and ethanolysis was also investigated under standard reaction conditions. The relative activity of lipase could be well maintained over twelve repeated cycles with ethyl acetate while it reached to zero by 6th cycle when ethanol was used as an acyl acceptor.     

Preparation of a novel hydrophobic affinity cryogel for adsorption of lipase and its utilization as a chromatographic adsorbent for fast protein liquid chromatography

In this study, we have prepared a hydrophobic cryogel for the chromatographic separation of lipase from its aqueous solutions including single protein and protein mixture and also Yarrowia lipolytica cell extract. N‐methacryloyl‐(l )‐phenylalanine methyl ester was used as a monomer to provide the hydrophobic character to the prepared cryogels. The highest adsorption capacity was observed at pH 5.0 at 0.5 mL min^?1 flow rate. The chromatographic separation of lipase was achieved from a binary mixture of lipase:bovine serum albumin (BSA) and lipase:lysozyme, and was also achieved from triple‐mixture of lipase:lysozyme:BSA by using fast protein liquid chromatography. Finally, lipase purification was performed from Yarrowia lipolytica cell extract used as a natural source. These studies have shown that the hydrophobic cryogel has good chromatographic performance for the separation and purification of lipase not only from aqueous solution, but also from cell extract as a natural source of lipase. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:376–382, 2014     

Isolation of stimulatory modulator of guanosine 3':5'-monophosphate-dependent protein kinase from mammalian heart devoid of inhibitory modulator of adenosine 3':5'-monophosphate-dependent protein kinase.

The stimulatory and inhibitory activities in the crude preparation of protein kinase modulator from dog heart were separated by Sephadex G-100 gel filtration, and the stimulatory modulator was further purified by DEAE-cellulose chromatography. The isolated stimulatory modulator, as the crude modulator preparation, stimulated the activity of the purified guanosine 3':5'-monophosphate (cGMP)-dependent protein kinases of both mammalian and arthropod origins in the presence of cGMP. The cGMP-dependent protein kinases were not activated by cGMP in the absence of either the isolated stimulatory modulator or the crude modulator. The stimulatory modulator, unlike the crude modulator had no effect on the activity of adenosine 3':5'-monophosphate (cAMP)-dependent protein kinase. The stimulatory modulator was a protein since its activity was destroyed by trypsin but was resistant to hydrolysis by DNase, RNase, phospholipase C, and lysozyme. The isolated inhibitory modulator, presumably the same as the protein inhibitor of cAMP-dependent protein kinase reported by Walsh et al. (Wash. D.A., Ashby, C.D., Gonzalez, C., Calkins, D., Fischer. E.H., and Krebs, E.G. (1971) J. Biol. Chem. 246, 1977-1985), depressed the cAMP-stimulated activity of cAMP-dependent protein kinase as did the crude preparation of protein kinase modulator. The isolated inhibitory modulator, unlike the crude preparation, was without effect on cGMP-dependent protein kinase. The present findings provide evidence to support that in mammals there are separate proteins for the stimulatory and the inhibitory activities of protein kinase modulator, in contrast to the modulator from an arthropod tissue (lobster tail muscle, Donnelly et al. (Donnelly, T.E., Jr., Kuo, J.F., Reyes, P.L., Liu, Y.P., and Greengard, P. (1973) J. Biol. Chem. 248, 190-198) which has been shown to possess both activities.     

The Effects of Surfactants on Lipase-Catalysed Hydrolysis of Esters: Activities and Stereoselectivity

The effect of surfactants on the hydrolysis of prochiral and chiral substrates by crude and purified porcine pancreatic lipase (PPL, EC 3.1.1.3)) has been studied. Rather than accelerating the reactions, surfactants slowed down (“inhibited”) the reactions relative to the rate in the absence of surfactant. Surfactants varied in the extent to which the reaction was inhibited. With the crude enzyme there was a correlation between degree of inhibition and the optical purity of the product of hydrolysis of an achiral diester substrate 1. There was no special effect associated with use of surfactants in the concentration range corresponding to critical micelle formation, nor was there any increase in rate of reaction when stable emulsions were formed by using mixtures of surfactants to generate an appropriate hydrophile-lipophile (HLB) balance. A study of the effect of sodium dodecyl sulphate (SDS) on the hydrolysis of the diester 1 by crude PPL showed that the rate of the reaction steadily decreased with increasing surfactant concentration, but that the optical purity of the product first fell and then rose gain, an effect attributed to the differential denaturing action of the surfactant on at least three hydrolytic enzymes. In general, there would seem to be no advantage to be gained from the use of surfactants in the hydrolysis by PPL of compounds of low water solubility; the use of an immiscible co-solvent is more effective.     

Surfactant-Modified lipase for the catalysis of the interesterification of triglycerides and fatty acids

The lipase-catalyzed intresterification of triglycerides and fatty acids in n-hexane was studied. Initially, lipase Saiken was modified with a surfactant of sorbitan esters so that its dispersibility in hydrophobic organic media was improved. The surfactant-modified lipase formed in the modification process carried out in a buffer solution has 1,3-positional specificity and predominantly catalyzed the interesterification reaction in a microaqueous n-hexane system. The modification technique converted inactive lipases to very active biocatalysts for the interesterification of triglycerides and fatty acids. The pH and the weight ratio of surfactant to enzyme used during the lipase modification process have shown significant effects in determining the recoveries of the protein and enzyme activity from the buffer solution, the protein content of the modified lipase complex after being freeze dried, and the interesterification activity of the complex. The water content in the reaction solution has strongly influenced the enzyme activity as well as the distribution of the products. (c) 1995 John Wiley & Sons, Inc.     

Enhanced reactivity of Rhizopus oryzae lipase displayed on yeast cell surfaces in organic solvents: potential as a whole-cell biocatalyst in organic solvents

Immobilization of enzymes on some solid supports has been used to stabilize enzymes in organic solvents. In this study, we evaluated applications of genetically immobilized Rhizopus oryzae lipase displayed on the cell surface of Saccharomyces cerevisiae in organic solvents and measured the catalytic activity of the displayed enzyme as a fusion protein with alpha-agglutinin. Compared to the activity of a commercial preparation of this lipase, the activity of the new preparation was 4.4 x 10(4)-fold higher in a hydrolysis reaction using p-nitrophenyl palmitate and 3.8 x 10(4)-fold higher in an esterification reaction with palmitic acid and n-pentanol (0.2% H2O). Increased enzyme activity may occur because the lipase displayed on the yeast cell surface is stabilized by the cell wall. We used a combination of error-prone PCR and cell surface display to increase lipase activity. Of 7,000 colonies in a library of mutated lipases, 13 formed a clear halo on plates containing 0.2% methyl palmitate. In organic solvents, the catalytic activity of 5/13 mutants was three- to sixfold higher than that of the original construct. Thus, yeast cells displaying the lipase can be used in organic solvents, and the lipase activity may be increased by a combination of protein engineering and display techniques. Thus, this immobilized lipase, which is more easily prepared and has higher activity than commercially available free and immobilized lipases, may be a practical alternative for the production of esters derived from fatty acids.     

Hydrolysis of butteroil by immobilized lipase using a hollow-fiber reactor: part I. lipase adsorption studies

Adsorption of proteins from a crude preparation containing a lipase from Aspergillus niger on microporous polypropylene hollow fibers was studied at six different temperatures. Langmuir isotherms accurately describe the overall adsorption equilibria. Lipase is selectively adsorbed relative to the other proteins in the crude preparation. Hence, immobilization also provides further purification of the lipase. The predictions of the Langmuir model for the change in the specific activity of lipase upon adsorption are consistent with experimental results. The loading capacity of the hollow fibers decreases and the adsorption constant increases as temperature is increased. This effect is more significant in the case of lipolytic activity than it is for the total amount of adsorbed protein. Small, positive enthalpy changes are associated with the adsorption of lipase on these hydrophobic membranes.     

Enzymatic purification of dihomo-γ-linolenic acid from Mortierella single-cell oil

Purification of dihomo-γ-linolenic acid (20:3n−6; DGLA) from a single-cell oil containing 39 wt.% DGLA was attempted. The process comprised: (i) non-selective hydrolysis of the oil to prepare a mixture of free fatty acids (FFAs); (ii) urea adduct fractionation of the FFA mixture to remove saturated fatty acids; and (iii) repeated selective esterification of the resulting mixture with two kinds of lipases. In the first step, Candida rugosa lipase (Lipase-OF from Meito Sangyo Co. Ltd., Aichi, Japan) was the most effective for preparation of the FFAs from the oil; 99% hydrolysis was achieved by the reaction at 40 °C for 72 h. Urea adduct fractionation of the FFA mixture removed almost completely behenic and lignoceric acids, and the content of DGLA increased from 39 to 55 wt.%. The FFAs were esterified with 2 mol equivalent of lauryl alcohol (LauOH) using C. rugosa lipase (Lipase-AY from Amano Enzyme Inc., Aichi, Japan). In consequent, DGLA was enriched to 86 wt.% in the unesterified FFA fraction. To further increase the content of DGLA, the esterification was repeated using the same lipase. Accordingly, the content of DGLA increased to 91 wt.%, but the preparation was contaminated with 3.3 wt.% γ-linolenic acid. This contaminant was removed finally by selective esterification of the FFAs with 2 mol equivalent of LauOH using Pseudomonas aeruginosa lipase. A series of procedures purified DGLA to 95 wt.% in a yield of 51% of the initial content in the single-cell oil.     

Characterization of lipase in reversed micelles formulated with cibacron blue F-3GA modified span 85

Sorbitan trioleate (Span 85) modified by Cibacron Blue F-3GA (CB) was prepared and used as an affinity surfactant to formulate a reversed micellar system for Candida rugosa lipase (CRL) solubilization. The system was characterized and evaluated by employing CRL-catalyzed hydrolysis of olive oil as a model reaction. The micellar hydrodynamic radius results reflected, to some extent, the redistribution of surfactant and water after enzyme addition, and the correlation between surfactant formulation, water content (W0), micellar size, and enzyme activity. An adequate modification density of CB was found to be important for the reversed micelles to retain enough hydration capacity and achieve high enzyme activity. Compared with the results in AOT-based reversed micelles, CRL in this micellar system exhibited a different activity behavior versus W0. The optimal pH and temperature of the encapsulated lipase remained unchanged, but the apparent activity was significantly higher than that of the native enzyme in bulk solution. Kinetic studies indicated that the encapsulated lipase in the reversed micelles of CB-formulated Span 85 followed the Michaelis-Menten equation. The Michaelis constant was found to decrease with increasing surfactant concentration, suggesting an increase of the enzyme affinity for the substrate. Stability of the lipase in the reversed micelles was negatively correlated to W0.     

Reverse micellar extraction for downstream processing of lipase: Effect of various parameters on extraction

Reverse micellar extraction of lipase using cationic surfactant cetyltrimethylammonium bromide (CTAB) was investigated. The effect of various process parameters on both forward and backward extraction of lipase from crude extract was studied to optimize its yield and purity. Forward extraction of lipase was found to be maximum using Tris buffer at pH 9.0 containing 0.10 M NaCl in aqueous phase and 0.20 M CTAB in organic phase consisting of isooctane, butanol and hexanol. In case of backward extraction, lipase was extracted from the organic phase to a fresh aqueous phase in 0.05 M potassium phosphate buffer (pH 7.0) containing 1.0 M KCl. The activity recovery, extraction efficiency and purification factor of lipase were found to be 82.72%, 40.27% and 4.09-fold, respectively. The studies also indicated that the organic phase recovered after back extraction could be reused for the extraction of lipase from crude extract.     

Separation and purification of lipase using reverse micellar extraction: Optimization of conditions by response surface methodology

Downstream processing of lipase involving reverse micellar extraction of lipase using cationic surfactant cetyltrimethylammonium bromide (CTAB) was investigated. Effect of various process parameters on both forward and backward extraction of lipase from crude extract was studied to optimize its yield and purity. Complex interaction of salt concentration (0.05∼0.15M), surfactant concentration (0.10∼0.30 M), and pH (6.0∼9.0) for forward extraction, as well as, salt concentration (0.5∼1.5 M) and pH (6.0∼9.0) for backward extraction have been studied using response surface methodology. Optimum processing conditions, namely, salt concentration 0.16M, surfactant concentration 0.20 M, and pH 9.0 for forward extraction, as well as, salt concentration 0.80 M and pH 7.23 for backward extraction, fulfill the conditions to obtain activity recovery of lipase ≥78% and purification factor of lipase ≥4.0. The study demonstrated that response surface methodology can be used for optimization of the conditions for reverse micellar extraction of lipase.     

Fatty acid preference of mycelium-bound lipase from a locally isolated strain of <Emphasis Type="Italic">Geotrichum candidum</Emphasis>

Mycelium-bound lipase (MBL) was prepared using a strain of Geotrichum candidum isolated from local soil. At the time of maximum lipase activity (54 h), the mycelia to which the lipase was bound were harvested by filtration and centrifugation. Dry MBL was prepared by lyophilizing the mycelia obtained. The yield of MBL was 3.66 g/l with a protein content of 44.11 mg/g. The lipase activity and specific lipase activity were 22.59 and 510 U/g protein, respectively. The moisture content of the MBL was 3.85%. The activity of free (extracellular) lipase in the culture supernatant (after removal of mycelia) was less than 0.2 U/ml. The MBL showed selectivity for oleic acid over palmitic acid during hydrolysis of palm olein, indicating that the lipase from G. candidum displayed high substrate selectivity for unsaturated fatty acid containing a cis-9 double bond, even in crude form. This unique specificity of MBL could be a direct, simple and inexpensive way in the fats and oil industry for the selective hydrolysis or transesterification of cis-9 fatty acid residues in natural triacylglycerols.     

A surfactant-coated lipase immobilized in magnetic nanoparticles for multicycle ethyl isovalerate enzymatic production

Gum arabic coated magnetic Fe₃O₄ nanoparticles (GAMNP) were prepared by chemical co-precipitation method and their surface morphology, particle size and presence of polymer-coating was confirmed by various measurements, including transmission electron microscopy (TEM), X-ray diffraction (XRD), thermo gravimetric analysis (TGA), and Fourier transform infra red (FTIR) analysis. Magnetic particles were employed for their potential application as a support material for lipase immobilization. Glutaraldehyde was used as a coupling agent for efficient binding of lipase onto the magnetic carrier. For this purpose, the surface of a Candida rugosa lipase was initially coated with various surfactants, to stabilize enzyme in its open form, and then immobilized on to the support. This immobilized system was used as a biocatalyst for ethyl isovalerate, a flavor ester, production. The influence of various factors such as type of surfactant, optimum temperature and pH requirement, organic solvent used, amount of surfactant in coating lipase and effect of enzyme loadings on the esterification reaction were systematically studied. Different surfactants were used amongst which non-ionic surfactant performed better, showing about 80% esterification yield in 48 h as compared to cationic/anionic surfactants. Enhanced activity due to interfacial activation was observed for immobilized non-ionic surfactant–lipase complex. The immobilized surfactant coated lipase activity was retained after reusing seven times.