Effect of immobilization support, water activity, and enzyme ionization state on cutinase activity and enantioselectivity in organic media

We studied the reaction between vinyl butyrate and 2-phenyl-1-propanol in acetonitrile catalyzed by Fusarium solani pisi cutinase immobilized on zeolites NaA and NaY and on Accurel PA-6. The choice of 2-phenyl-1-propanol was based on modeling studies that suggested moderate cutinase enantioselectivity towards this substrate. With all the supports, initial rates of transesterification were higher at a water activity (a(w)) of 0.2 than at a(w) = 0.7, and the reverse was true for initial rates of hydrolysis. By providing acid-base control in the medium through the use of solid-state buffers that control the parameter pH-pNa, which we monitored using an organo-soluble chromoionophoric indicator, we were able, in some cases, to completely eliminate dissolved butyric acid. However, none of the buffers used were able to improve the rates of transesterification relative to the blanks (no added buffer) when the enzyme was immobilized at an optimum pH of 8.5. When the enzyme was immobilized at pH 5 and exhibited only marginal activity, however, even a relatively acidic buffer with a pK(a) of 4.3 was able to restore catalytic activity to about 20% of that displayed for a pH of immobilization of 8.5, at otherwise identical conditions. As a(w) was increased from 0.2 to 0.7, rates of transesterification first increased slightly and then decreased. Rates of hydrolysis showed a steady increase in that a(w) range, and so did total initial reaction rates. The presence or absence of the buffers did not impact on the competition between transesterification and hydrolysis, regardless of whether the butyric acid formed remained as such in the reaction medium or was eliminated from the microenvironment of the enzyme through conversion into an insoluble salt. Cutinase enantioselectivity towards 2-phenyl-1-propanol was indeed low and was not affected by differences in immobilization support, enzyme protonation state, or a(w).     

Working at controlled water activity in a continuous process: the gas/solid system as a solution

Fusarium solani cutinase and Candida cylindracea lipase were used to catalyze a transesterification reaction in a continuous gas/solid bioreactor. In this system, a solid phase composed of a packed enzymatic preparation was continuously percolated with carrier gas which fed substrate and removed reaction products simultaneously. Different conditions of immobilization were used and compared to the results obtained with a nonsupported enzyme. The enzymatic activity was found to be highly dependent of a key parameter: water activity (a(w)). Biocatalyst stability was greatly influenced by water activity and the choice of immobilization technique for the enzymatic material. For free and adsorbed enzymes, water requirements exhibited optima which corresponded to the complete hydration coverage of the protein. These optima presented a good correlation with the isotherm sorption curves obtained for the different preparations. In this work are reported the results concerning the possibility of using a continuous system able to operate at controlled water activity in a heterogeneous medium. Lipolytic enzyme in such a system appears to be a new process for the biotransformation of volatile esters. (c) 1995 John Wiley & Sons, Inc.     

Kinetics and mechanism of the cutinase-catalyzed transesterification of oils in AOT reversed micellar system

The kinetics of the enzymatic transesterification between a mixture of triglycerides (oils) and methanol for biodiesel production in a bis(2-ethylhexyl) sodium sulfosuccinate (AOT)/isooctane reversed micellar system, using recombinant cutinase from Fusarium solani pisi as a catalyst, was investigated. In order to describe the results that were obtained, a mechanistic scheme was proposed, based on the literature and on the experimental data. This scheme includes the following reaction steps: the formation of the active enzyme–substrate complex, the addition of an alcohol molecule to the complex followed by the separation of a molecule of the fatty acid alkyl ester and a glycerol moiety, and release of the active enzyme. Enzyme inhibition and deactivation effects due to methanol and glycerol were incorporated in the model. This kinetic model was fitted to the concentration profiles of the fatty acid methyl esters (the components of biodiesel), tri-, di- and monoglycerides, obtained for a 24 h transesterification reaction performed in a stirred batch reactor under different reaction conditions of enzyme and initial substrates concentration.     

Thiol-functionalization of acrylic ester monomers catalyzed by immobilized Humicola insolens cutinase

Immobilized cutinase HiC from the ascomycete Humicola insolens was applied as a novel biocatalyst for the synthesis of functionalized acryclic esters by transesterification. As a model reaction, transesterification of methyl acrylate with 6-mercapto-1-hexanol at a high molar ratio in a solvent free system was chosen. Besides two minor Michael-addition by-products, 6-mercaptohexyl acrylic ester was identified as the main product with the thiol as the functional end group. Reaction conditions were optimized regarding the influence of water (0-1.72 M), temperature (22-50 °C), product inhibition and addition of the radical inhibitor butylated hydroxytoluol (BHT; 0.14-0.71 M) on conversion and by-product formation. Highest conversion of 6-mercapto-1-hexanol to 6-mercaptohexyl acrylic ester (95.4 ± 0.3%) was achieved after 6h at 40 °C in the presence of 0.025% (w/w) water without formation of by-products in a solvent free system. Applying methyl methacrylate, transesterification with 6-mercapto-1-hexanol was significantly lower (43.6 ± 0.1%) compared to transesterification of methyl acrylate with 6-mercapto-1-hexanol.     

Gas phase transesterification reactions catalyzed by lipolytic enzymes

Porcine pancreatic lipase and Fusarium solani cutinase were used to catalyze transesterification reactions between methyl propionate, ethyl propionate, and a series of primary alcohols at high temperatures in a continuous packed-bed gas-solid reactor, in which the solid phase is composed of the enzyme and the substrates and products are in a gaseous form. In this type of system, enzyme activity was found to depend essentially on the water activity (A(w)) of the enzyme preparation.     

Methanolysis of cholesteryl esters: conditions for quantitative preparation of methyl esters.

We have investigated the conditions required to obtain a quantitative yield of methyl esters from cholesteryl esters by alkaline methanolysis. Methanolysis of the cholesteryl ester for 60 min at room temperature with 1 m methoxide reagent ensured complete reaction. Some ester hydrolysis always accompanied methanolysis and necessitated acid-catalyzed methylation of the resultant fatty acids after completion of the alcoholysis. Analysis of the composition of methyl ester product and remaining cholesteryl ester substrate before methanolysis had gone to completion showed selective hydrolysis of some fatty acid cholesteryl esters and illustrates the importance of obtaining a quantitative yield of methyl esters following methanolysis.     

Hydrolysis of plant cuticle by plant pathogens. Properties of cutinase I, cutinase II, and a nonspecific esterase isolated from Fusarium solani pisi.

The properties of the homogeneous cutinase I, cutinase II, and the nonspecific esterase isolated from the extracellular fluid of cutin-grown Fusarium solani F. pisi (R.E. Purdy and P.E. Kolattukudy (1975), Biochemistry, preceding paper in this issue) were investigated. Using tritiated apple cutin as substrate, the two cutinases showed similar substrate concentration dependence, protein concentration dependence, time course profiles, and pH dependence profiles with optimum near 10.0. Using unlabeled cutin, the rate of dihydroxyhexadecanoic acid release from apple fruit cutin by cutinase I was determined to be 4.4 mumol per min per mg. The cutinases hydrolyzed methyl hexadecanoate, cyclohexyl hexadecanoate, and to a much lesser extent hexadecyl hexadecanoate but not 9-hexadecanoyloxyheptadecane, cholesteryl hexadecanoate, or hexadecyl cinnamate. The extent of hydrolysis of these model substrates by cutinase I was at least three times that by cutinase II. The nonspecific esterase hydrolyzed all of the above esters except hexadecyl cinnamate, and did so to a much greater extent than did the cutinases. None of the enzymes hydrolyzed alpha- or beta-glucosides of p-nitrophenol. p-Nitrophenyl esters of fatty acids from C2 through C18 were used as substrates and V's and Kms were determined...     

Kinetics and modelling of an alcoholysis reaction catalyzed by cutinase immobilized on NaY zeolite

Fusarium solani pisi recombinant cutinase was immobilized by adsorption on NaY zeolite. The kinetics of the alcoholysis reaction of butyl acetate with hexanol in isooctane catalyzed by cutinase immobilized on NaY zeolite, was studied. The reaction kinetics is suggested to follow a Ping-Pong bi–bi mechanism in which competitive inhibition by excess of alcohols has been identified. No evidence of any significant external diffusional limitation has been detected. The time validation of the model was successfully achieved simultaneously for 15 experimental product evolutions in a batch stirred tank reactor (BSTR) for different initial reactant concentrations.     

Effects of ionic surfactants used in reversed micelles on cutinase activity and stability

The effects of aqueous surfactant solutions on the kinetics and stability of cutinase from Fusarium solani pisi were studied. The surfactant sodium bis[2-ethylhexyl]ester sulfosuccinic acid (AOT) acts as a pseudo-competitive inhibitor within a limited concentration range relative to the hydrolysis of short-chain p-nitrophenyl esters. For higher concentrations a hyperbolic mixed inhibition takes place. A pseudo-activation of hydrolysis in presence of AOT and hexadecyltrimethyl-ammonium bromide (CTAB) was observed. CTAB has similar effects on kinetics of cutinase. Cutinase revealed to be stable in CTAB solutions, with activity retention as high as 80%. AOT has a deleterious effect on the enzyme in the time course, resulting in acute loss of activity possibly related with unfolding of the protein structure. A relation between deactivation rate constants and AOT/cutinase concentration ratios is suggested. The presence of the linear alcohol, 1-hexanol, was included in these solutions, in the attempt to interpret the deactivation of cutinase when encapsulated in reversed micelle systems in the absence of this co-surfactant.     

Single-cell protein production from ram horn hydrolysate by bacteria

The alcoholysis (transesterification) of the refined cotton seed oil of Turkish origin with primary and secondary alcohols was investigated in the presence of an immobilized enzyme from Candida antarctica, commercially called Novozym 435 in a solvent-free medium. The optimum conditions of the methanolysis were as follows: 30% enzyme based on oil weight; oil/alcohol molar ratio 1:4; temperature: 50 degrees C and reaction time: 7 h. Maximum methyl esters (ME) yield was 91.5%. At the same conditions cotton seed oil was converted with short-chain primary and secondary alcohols to its corresponding esters with conversions between 72% and 94%. Our results indicated that alcoholysis products of cotton seed oil could be used as valuable intermediates in oleochemistry.     

Cutinase: from molecular level to bioprocess development

This review analyzes the role of cutinases in nature and their potential biotechnological applications. The cloning and expression of a fungal cutinase, Fusarium solani f. pisi, in Escherichia coli and Saccharomyces cerevisiae hosts are described. The three-dimensional structure of this cutinase is also analyzed and its function as a lipase is discussed and compared with other lipases. The biocatalytic applications of cutinase are described taking into account the preparation of different cutinase forms and the media in which the different types of reactions have been performed, namely hydrolysis, esterification, transesterification, and resolution of racemic mixtures. The stability of cutinase preparations is discussed and, in particular, the cutinase stability in anionic reversed micelles is analyzed considering the role of hexanol as a substrate, a cosurfactant, and a stabilizer. Process development, based on the operation of cutinase reactors, is also reviewed.     

Optimized enzymatic synthesis of ascorbyl esters from lard using Novozym 435 in co-solvent mixtures

A mild and efficient method for the conversion of fatty acid methyl esters from lard into ascorbyl esters via lipase-catalyzed transesterification in co-solvent mixture is described. A solvent engineering strategy was firstly applied to improve fatty acid ascorbyl esters production. The co-solvent mixture of 30% t-pentanol:70% isooctane (v/v) was optimal. Response surface methodology (RSM) and central composite design (CCD) were employed to estimate the effects of reaction parameters, such as reaction time (12–36 h), temperature (45–65 °C), enzyme amount (10–20%, w/w, of fat acid methyl esters), and substrate molar ratio of fatty acid methyl esters to ascorbic acid (8:1–12:1) for the synthesis of fatty acid ascorbyl esters in co-solvent mixture. Based on the RSM analysis, the optimal reaction conditions were determined as follows: reaction time 34.32 h, temperature 54.6 °C, enzyme amount 12.5%, substrate molar ratio 10.22:1 and the maximum conversion of fatty acid ascorbyl esters was 69.18%. The method proved to be applicable for the synthesis of ascorbyl esters using Novozym 435 in solvent.     

On the Acaciin

Synthesis of N-2,2,3,3-tetrafluoropropionyl-amino acids (abbreviated as tetrafluoropropionyl- or Tfp-amino acids) by the reaction of amino acids with tetrafluoropropionyl anhydride was described, Racemization was observed to occur to a considerable extent during the process of the introduction of this group. Optically active Tfp-amino acids were able to be prepared free from racemization by transesterification of methyl tetrafluoropropionate with amino acid tert-butyl esters, followed by treatment of the resulting Tfp-amino acid tert-butyl esters with trifluoroacetic acid. Some Tfp-dipeptide esters were prepared from the corresponding dipeptide tert-butyl esters in this way. This group was cleavable by mild alkaline hydrolysis or by reduction with sodium borohydrde as well as the Tfa-group.     

Solid/gas biocatalysis: How to fully define the system ?

Summary Fusarium solani cutinase supported on Chromosorb P was used to catalyse transesterification and hydrolytic reactions of short volatile alcohols and esters in a continuous gas/solid bioreactor. We showed that it was of great importance to take into account the thermodynamic activity of each chemical species present in the system, related to the effective availability of the substrates (and/or products).     

Isolation and characterization of a cutinase from Fusarium roseum culmorum and its immunological comparison with cutinases from F. solani pisi.

Fusarium roseum culmorum, grown on apple cutin as the sole source of carbon, was shown to produce a cutin depolymerizing enzyme. From the extracellular fluid of these F. roseum cultures, a cutinase and a nonspecific esterase were isolated utilizing Sephadex G-100, QAE-Sephadex, and SP-Sephadex chromatography. The homogeneity of the cutinase was verified by polyacrylamide disc gel electrophoresis. The molecular weight of the cutinase was estimated to be 24,300 by polyacrylamide gel electrophoresis in the presence of sodium dodecyl sulfate. Electrophoretic mobility of this enzyme was between that of Cutinases I and II from Fusarium solani pisi. The F. roseum cutinase hydrolyzed p-nitrophenyl butyrate and cutin, but not p-nitrophenyl palmitate, while the nonspecific esterase hydrolyzed the long-chain esters. Amino acid composition of F. roseum cutinase was found to be similar to that of F. solani pisi Cutinase I except for differences in the number of serine, valine, and cysteine residues. The time-course, protein concentration dependence, substrate concentration dependence, and pH optimum (10.0 for cutin hydrolysis) of the F. roseum cutinase was similar to the cutinases from F. solani pisi. The F. roseum cutinase was inhibited by diisopropylfluorophosphate and paraoxon, and the [³H]diisopropylphosphate group was covalently attached to the enzyme upon treatment with tritiated diisopropylfluorophosphate. Therefore, it is concluded that catalysis by cutinase involves an “active serine.” Immunochemical studies with a rabbit antibody prepared against F. solani pisi Cutinase I demonstrated that Cutinase II from this organism was immunologically very similar to, but not identical to, Cutinase I. On the other hand, the cutinase from F. roseum was immunologically quite different from the cutinases isolated from F. solani pisi in that it did not cross-react with anticutinase I. However, all three cutinases were virtually identical in their sensitivity to inhibition by anticutinase I, and all three enzymes were virtually completely inhibited by the anticutinase I.     

2-Ethyl-1-hexanol fatty acid esters from rapeseed oil by transesterification

Summary Fatty acid esters of 2-ethyl-1-hexanol were produced in a small pilot scale from rapeseed oil by Candida cylindracea lipase catalyzed transesterification (alcoholysis) without added solvent. Up to 90% conversion of rapeseed oil (97% of theoretical) was obtained in 8 h in 2 kg scale at 37° C with 3.4% (w/w) lipase immobilized on an anion exchange resin Amberlite XAD-7, rapeseed oil:2-ethyl-1-hexanol substrate molar ratio of 2.8, and 3% (w/w) of added water.     

Kinetics of lipase-catalysed methyl gallate production in the presence of deep eutectic solvent

Production of methyl gallate (MG), which is an important phenolic acid ester for pharmaceutical industry, was carried out by Novozym 435-catalysed transesterification of propyl gallate (PG) with methanol in a deep eutectic solvent. Reaction parameters governing substrate molar ratio, enzyme concentration, temperature and agitation rate were investigated batch-wise in choline chloride:glycerol-water binary mixture. The results were evaluated in terms of conversion of PG, yield of MG and hydrolysis of PG to gallic acid. 10% (w/w) of water was found to be favourable in the reaction medium for low hydrolysis percent. The highest conversion (17.4%) and yield (60.4%) but the lowest hydrolysis (2%) after 120?h of transesterification were found at PG/methanol molar ratio of 1:6, enzyme concentration of 40?g/L, 50?°C and 200?rpm. A kinetic model based on the Ping-Pong Bi–Bi mechanism for transesterification of PG was proposed with the assumption that there were no internal and external mass transfer resistances.     

Interfacial binding of cutinase rather than its catalytic activity determines the steady state interfacial tension during oil drop lipid hydrolysis

Hydrolysis of triglycerides by cutinase from Fusarium solani pisi causes in oil drop tensiometer experiments a decrease of the interfacial tension. A series of cutinase variants with amino acid substitutions at its molecular surface yielded different values of the steady state interfacial tension. This tension value poorly correlated with the specific activity as such nor with the total activity (defined as the specific activity multiplied by the amount of enzyme bound) of the cutinase variants. Moreover, it appeared that at activity levels above 15% of that of wild type cutinase the contribution of hydrolysis to the decrease of the tension is saturating. A clear positive correlation was found between the interfacial tension plateau value and the interfacial binding of cutinase, as determined with attenuated total reflection Fourier transformed infrared spectroscopy (ATR-FTIR). These results indicate that the interfacial steady state level is not determined by the rate of hydrolysis, but mainly by the interfacial binding of cutinase.     

Substrate specificity and kinetic properties of enzymes belonging to the hormone-sensitive lipase family: comparison with non-lipolytic and lipolytic carboxylesterases

We have studied the kinetics of hydrolysis of triacylglycerols, vinyl esters and p-nitrophenyl butyrate by four carboxylesterases of the HSL family, namely recombinant human hormone-sensitive lipase (HSL), EST2 from Alicyclobacillus acidocaldarius, AFEST from Archeoglobus fulgidus, and protein RV1399C from Mycobacterium tuberculosis. The kinetic properties of enzymes of the HSL family have been compared to those of a series of lipolytic and non-lipolytic carboxylesterases including human pancreatic lipase, guinea pig pancreatic lipase related protein 2, lipases from Mucor miehei and Thermomyces lanuginosus, cutinase from Fusarium solani, LipA from Bacillus subtilis, porcine liver esterase and Esterase A from Aspergilus niger. Results indicate that human HSL, together with other lipolytic carboxylesterases, are active on short chain esters and hydrolyze water insoluble trioctanoin, vinyl laurate and olive oil, whereas the action of EST2, AFEST, protein RV1399C and non-lipolytic carboxylesterases is restricted to solutions of short chain substrates. Lipolytic and non-lipolytic carboxylesterases can be differentiated by their respective value of K(0.5) (apparent K(m)) for the hydrolysis of short chain esters. Among lipolytic enzymes, those possessing a lid domain display higher activity on tributyrin, trioctanoin and olive oil suggesting, then, that the lid structure contributes to enzyme binding to triacylglycerols. Progress reaction curves of the hydrolysis of p-nitrophenyl butyrate by lipolytic carboxylesterases with lid domain show a latency phase which is not observed with human HSL, non-lipolytic carboxylesterases, and lipolytic enzymes devoid of a lid structure as cutinase.