Solvent-free enzymatic synthesis of fatty alkanolamides

An environmentally benign and volume efficient process for enzymatic production of alkanolamides is described. Immobilized Candida antarctica lipase B, Novozym435, was used to catalyze the condensation of lauric acid with monoethanolamine. The reaction temperature of 90 degrees C was required to keep the reactants in a liquid state. Stepwise addition of the amine minimized problems caused by the formation of a highly viscous amine/fatty acid ion-pair. The enzyme was both very active and stable under the reaction conditions, with about half of the activity remaining after 2 weeks. The maximum amide yield obtained when using equimolar amounts of the reactants was 75%, which could be increased to 95% upon water removal. Special precautions to avoid co-distillation of the amine were required. Two different strategies to avoid the amine loss are presented.     

Preparation of eutectic substrate mixtures for enzymatic conversion of ATC to l-cysteine at high concentration levels

High concentration eutectic substrate solutions for the enzymatic production of l-cysteine were prepared. Eutectic melting of binary mixtures consisting of d,l-2-amino-Δ²-thiazoline-4-carboxylic acid (ATC) as a substrate and malonic acid occurred at 39 °C with an ATC mole fraction of 0.5. Formation of eutectic mixtures was confirmed using SEM, SEM–EDS, and XPS surface analyses. Sorbitol, MnSO₄, and NaOH were used as supplements for the enzymatic reactions. Strategies for sequential addition of five compounds, including a binary ATC mixture and supplements, during preparation of eutectic substrate solutions were established. Eutectic substrate solutions were stable for 24 h. After 6 h of enzymatic reactions, a 550 mM l-cysteine yield was obtained from a 670 mM eutectic ATC solution.     

Solvent-free enzymatic synthesis of feruloylated diacylglycerols and kinetic study

The enzymatic esterification of glyceryl ferulate (FG) and oleic acid (OA) for feruloylated diacylglycerols (FDAG) synthesis in a solvent-free system was studied in this work. The reactions were catalyzed by different commercially available lipases, among which Novozym 435 was found to be the most active biocatalyst. The effects of glycerol in the reaction mixture and various synthesis parameters on yield of FDAG and the initial reaction rate were studied. The optimum synthesis conditions were as follows: temperature, 65 °C; enzyme load, 7.5%; substrate ratio, 7.5:1 (OA/(FG + glycerol), w/w); and reaction time, 12 h. Under the optimum conditions, the conversion of FG and yield of FDAG reached 98.0 ± 1.0% and 82.6 ± 2.2%, respectively. A linear relationship was established between the initial reaction rate and enzyme load up to 10%, which demonstrated that the influence of external mass transfer limitations on the reaction could be eliminated. The relationship between initial reaction rate and temperature was also established, based on the Arrhenius law. Novozym 435 in the present work can be used 18 times under the optimum conditions without essential losses in activity. The reaction kinetics agrees with the Ping-Pong Bi-Bi mechanism characterized by V_m and K^′_m values of 5.26 × 10⁻⁴ mol/(L min) and 0.26 mol/L, respectively.     

Quantitative analysis of enzymatic fractionation of multiple substrate mixtures

The enzymatic conversion of mixtures of multiple substrates was studied quantitatively, based on established methodology used for the enzymatic kinetic resolution of racemic mixtures, involving the use of competitive factors: ratios of specificity constants (k_cat/K_M) of substrate pairs. The competitive factors of the substrates were defined in relation to a reference substrate. These competitive factors were used to predict the composition of the reaction mixture as a function of the degree of conversion of the reaction. The methodology was evaluated using three different lipases to hydrolyze a model mixture of four fatty acid methyl esters and for the esterification of a mixture of the same fatty acids in free form with ethanol. In most cases, the competitive factors determined from the initial phase of the reactions predicted the product composition during the rest of the reaction very well. The slowest reacting fatty acid was erucic acid (both in free form and as methyl ester), which was thus enriched in the remaining substrate fraction, while the other fatty acids: lauric acid, palmitic acid and oleic acid were converted faster. Simulations of the compositions of reaction mixtures with different values of the competitive factors were carried out to provide an overview of what could be achieved using enzymatic enrichment. Possible applications include reactions involving homologous substrates and mixtures of multiple isomers. The analysis presented provides guidelines that can be useful in the screening and development of enzymes for enzymatic enrichment applications. Biotechnol. Bioeng. 2013; 110: 78–86. © 2012 Wiley Periodicals, Inc.     

Kinetically controlled enzymatic synthesis of dipeptide precursor of L-alanyl-L-glutamine

An important nutritional dipeptide precursor, benzoyloxycarbonyl protected L-alanyl-L-glutamine (Z-Ala-Gln), was successfully prepared through a kinetically controlled enzymatic peptide synthesis method. A commercially available and low-cost protease (papain) was used as biocatalyst with Z-Ala-OMe and Gln as acyl donor and nucleophile, respectively. The dipeptide yield was 35.5% under the optimized reaction conditions: 35°C, pH 9.5, and the ratio of acyl donor/nucleophile is 1:10. Based on the reaction mechanism and experimental data, the kinetic model was established, which was in accordance with the Michaelis-Menten equation, and the apparent Michaelis constant K(m)(app) and the apparent maximum reaction rate r(max)(app) were calculated as 1.71 mol/L and 6.09 mmol/(L Min), respectively.     

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.     

Protease-catalyzed synthesis of oligopeptides in heterogenous substrate mixtures

A systematic study of enzymatic peptide synthesis in heterogeneous substrate mixtures was carried out, with the aim of establishing the preparative scope of this methodology. Semiliquid eutectics were obtained with various combinations of neutral, acidic, and basic amino acid derivatives, in the presence or absence of adjuvants. A range of serine cysteine, and metalloproteases readily catalyzed the formation of the required dipeptides under these conditions. The synthetic usefulness of the approach was demonstrated by the sequential and convergent synthesis of derivatives of a number of bioactive di-, tri-, and pentapeptides, including aspartame, sweet lysine peptide, kyotorphin amide, ACE-inhibiting and -immunoactive tripeptides, and Leu-enkephalin amide, with overallyields of 21% to 84% and productivities of 0.13 to 0.75 g/g being obtained. (c) 1994 John Wiley & Sons, Inc.     

Solvent-free enzymatic synthesis of 1,3-diconjugated linoleoyl glycerol optimized by response surface methodology

An operation mode with N(2) bubbling under vacuum was employed for the solvent-free synthesis of 1,3-diconjugated linoleoyl glycerol (1,3-dCLG) from conjugated linoleic acid (CLA) catalyzed by Novozym 435. The response surface methodology (RSM) was adopted for the optimization of the reaction conditions with five major factors (incubation time, temperature, enzyme load, substrate mole ratio, and system vacuum) and three responses (CLA conversion, 1,3-dCLG yield, and acyl migration). Two sets of optimal conditions were recommended. Validation of the RSM model was verified by the good agreement between the experimental and the predicted values of 1,3-dCLG yield. Under the optimal conditions, the yield of 1,3-dCLG up to 93% was obtained. The reaction was scaled up to a production level of 100 g of 1,3-dCLG at a yield of 90.7%, indicating a promising feature of the technology in industrial applications.     

Solvent-free synthesis of glyceryl ferulate using a commercial microbial lipase

A process was optimized for the enzymatic synthesis of glyceryl ferulate with a yield of up to 96% using a vacuum-rotary evaporation strategy under following conditions: 15 mmol glycerol, 1.5 mmol ethyl ferulate, 170 mg Candida antarctica lipase, at 60°C for 10 h and under a vacuum of 10 mm Hg. The immobilized lipase can be used 10 times.     

Solvent-free geranyl oleate production by enzymatic esterification

This study reports the maximization of geranyl oleate production by esterification of geraniol and oleic acid in a solvent-free system using a commercial lipase as catalyst. The operating conditions that maximized geranyl oleate production were determined to be 40 °C, geraniol to oleic acid molar ratio of 5:1, 150 rpm and 10 wt% of enzyme, with a resulting reaction conversion of about 93%. After determining the best reaction parameters, a kinetic study was performed and the results obtained in this step allow to conclude that an excess of alcohol (alcohol to acid molar ratio of 5:1), relatively low enzyme concentration (5 wt%) and temperature of 50 °C afforded nearly complete reaction conversion after 1 h of reaction. New experimental data on enzymatic esterification of geraniol and oleic acid for geranyl oleate production are reported in this work, showing a promising perspective of the technique to overcome the inconvenience of the chemical-catalyzed route.     

Solvent-free enzymatic production of high quality cetyl esters

A solvent-free biocatalytic process for the synthesis of high quality cetyl laurate, myristate, palmitate and stearate has been optimized. This enzymatic procedure follows the fundamental principles of the Green Chemistry and lead to sustainable products, which can be labeled as natural and conform to the principal requirements for its use in high value-added goods. The four esters selected are the main components of spermaceti, a mixture of waxes very appreciated in cosmetic and pharmacy because of its physical properties and emolliency, which was formerly extracted from the head of the sperm whales. In this paper, the influence of the amount of biocatalyst, the commercially available Novozym^® 435, and the temperature were studied in an open-air batch reactor before carrying out the synthesis in a high performance vacuum reactor with dry nitrogen input to shift the equilibrium towards product formation. Under optimal conditions, conversion was higher than 98.5 %. The characterization of the enzymatic cetyl esters puts in evidence that these are ultra-pure compounds, which have similar properties to the ones obtained through the conventional industrial processes with the extra benefit of being environmentally friendly.     

Stereoselective enzymatic synthesis of an aspartame precursor of N-CBZ- -Asp- -PheOMe

A stereoselective protease produced by Bacillus amyloliquefaciens KCCM 12091 was isolated. The enzyme catalyzed the synthesis of N-CBZ- -Asp-PheOMe from N-CBZ- -Asp and -PheOMe, but not N-CBZ- -Asp- -PheOMe from N-CBZ- -Asp and -PheOMe. More than 50% of added -PheOMe was consumed when eutectic mixtures of N-CBZ- -Asp, racemic - and -PheOMe were used for synthesis of an aspartame precursor of N-CBZ- -Asp- -PheOMe. -PheOMe was not involved in the reaction and did not affect synthesis of N-CBZ- -Asp- -PheOMe.     

Rapid optimization of enzyme substrates using defined substrate mixtures.

A strategy is described for the rapid optimization of kcat/Km for protease substrates. Selected positions of a given peptide substrate sequence are varied through synthesis with mixtures of amino acids. Incubation of the resulting peptide mixture with the enzyme of interest and analysis by high pressure liquid chromatography provides a direct measure of analogs with enhanced kcat/Km. High performance liquid chromatography/continuous flow fast atom bombardment mass spectrometry is used to assign structure to each peak in the chromatogram. As an example of the utility and efficiency of "substrate mapping" we describe optimization of the collagenase substrate Dnp-Pro-Leu-Gly-Leu-Trp-Ala-D-Arg-NH2 (where Dnp is dinitrophenyl) at the P'1 and P'2 positions. Six different mixtures were prepared for evaluation, representing the synthesis of 128 different synthetic substrates. "Substrate mapping" has led to Dnp-Pro-Leu-Gly-Cys(Me)-His-Ala-D-Arg-NH2, a substrate that possesses a 10-fold better kcat/Km than Dnp-Pro-Leu-Gly-Leu-Trp-Ala-D-Arg-NH2.     

Modeling of the enzymatic kinetic synthesis of cephalexin--influence of substrate concentration and temperature

During enzymatic kinetic synthesis of cephalexin, an activated phenylglycine derivative (phenylglycine amide or phenylglycine methyl ester) is coupled to the nucleus 7-aminodeacetoxycephalosporanic acid (7-ADCA). Simultaneously, hydrolysis of phenylglycine amide and hydrolysis of cephalexin take place. This results in a temporary high-product concentration that is subsequently consumed by the enzyme. To optimize productivity, it is necessary to develop models that predict the course of the reaction. Such models are known from literature but these are only applicable for a limited range of experimental conditions. In this article a model is presented that is valid for a wide range of substrate concentrations (0-490 mM for phenylglycine amide and 0-300 mM for 7-ADCA) and temperatures (273-298 K). The model was built in a systematic way with parameters that were, for an important part, calculated from independent experiments. With the constants used in the model not only the synthesis reaction but also phenylglycine amide hydrolysis and cephalexin hydrolysis could be described accurately. In contrast to the models described in literature, only a limited number (five) of constants was required to describe the reaction at a certain temperature. For the temperature dependency of the constants, the Arrhenius equation was applied, with the constants at 293 K as references. Again, independent experiments were used, which resulted in a model with high statistic reliability for the entire temperature range. Low temperatures were found beneficial for the process because more cephalexin and less phenylglycine is formed. The model was used to optimize the reaction conditions using criteria such as the yield on 7-ADCA or on activated phenylglycine. Depending on the weight of the criteria, either a high initial phenylglycine amide concentration (yield on 7-ADCA) or a high initial 7-ADCA concentration (yield on phenylglycine amide) is beneficial.     

Comparative study of the enzymatic synthesis of cephalexin at high substrate concentration in aqueous and organic media using statistical model

Synthesis of cephalexin with immobilized penicillin acylase at high substrates concentration at an acyl donor to nucleophile molar ratio of 3 was comparatively evaluated in aqueous and ethylene glycol media using a statistical model. Variables under study were temperature, pH and enzyme to substrate ratio and their effects were evaluated on cephalexin yield, ratio of initial rates of cephalexin synthesis to phenylglycine methyl ester hydrolysis, volumetric and specific productivity of cephalexin synthesis, that were used as response parameters. Results obtained in both reaction media were modeled using surface of response methodology and optimal operation conditions were determined in terms of an objective function based on the above parameters. At very high substrates concentrations the use of organic co-solvents was not required to attain high yields and actually almost stoichiometric yields were obtained in a fully aqueous media with the advantages of higher productivities than in an organic co-solvent media and compliance with the principles of green chemistry.     

A method for the enzymatic synthesis and HPLC purification of the peptidoglycan precursor UDP-N-acetylmuramic acid

UDP-N-acetylmuramic acid (UDP-MurNAc) is a precursor for peptidoglycan biosynthesis in bacteria. A major difficulty in the study of this pathway is that UDP-MurNAc is not commercially available. We have developed an enzymatic synthesis scheme for UDP-MurNAc using two easily purified Escherichia coli polyhistidine tagged peptidoglycan biosynthesis enzymes, MurZ and MurB, followed by a single-step purification of UDP-MurNAc by high-performance liquid chromatography. The identity of the UDP-MurNAc synthesized by our method was confirmed by electrospray ionization mass spectrometry. Furthermore, we show that the UDP-MurNAc can support a UDP-MurNAc-L-alanine ligase reaction.     

Partition and substrate concentration effect in the enzymatic synthesis of cephalexin in aqueous two-phase systems

The kinetically controlled synthesis of cephalexin in aqueous two-phase systems was studied, using immobilized penicillin acylase, 7-amino 3-desacetoxycephalosporanic acid as nucleophile and phenylglycine methyl ester as acyl donor. The organic phases used were 80% (v/v) polyethyleneglycol 400 and 600 and the aqueous phase was 2.5 M (NH₄)₂SO₄. 7-amino 3-desacetoxycephalosporanic acid and cephalexin partition coefficients were determined at pH 7.4 and 7.8, at 14 °C and 20 °C. Highest partition coefficient for cephalexin was obtained for polyethyleneglycol 400–(NH₄)₂SO₄ at pH 7.4 and 20 °C, while the lowest partition coefficient for 7-amino desacetoxycephalosporanic acid was obtained in the same system at pH 7.8 and 14 °C. No significant effect of pH was observed on conversion yield and productivity of cephalexin synthesis; however, higher values were obtained with polyethyleneglycol 400 as organic phase. Higher conversion yields with both biphasic systems were obtained at the lowest temperature, where product hydrolysis was lower; volumetric productivity was higher for the fully aqueous medium (control), being higher at 20 °C. All parameters of synthesis were improved at higher substrates concentrations, obtaining conversion yields of 78.2% and 65.4%, with 60 mM 7-amino desacetoxycephalosporanic acid for the polyethyleneglycol 400–(NH₄)₂SO₄ system and the control, respectively.     

Feruloyl esterase-catalysed synthesis of glycerol sinapate using ionic liquids mixtures

The ability of a feruloyl esterase (AnFaeA), either in free or immobilised (cross-linked enzyme aggregates) form, to catalyse the esterification of glycerol, a major by-product of the biodiesel industry, with sinapic acid was studied in four hexafluorophosphate anion-containing ionic liquids: ([Bmim][PF(6)], [Omim][PF(6)], [C(2)OHmim][PF(6)] and [C(5)O(2)mim][PF(6)]). Such ionic liquids are considered 'green' reaction systems. The synthetic reaction was optimised in [C(2)OHmim][PF(6)] and the highest conversion yield was 72.5+/-2.1%, while, at the same reaction conditions in [C(5)O(2)mim] [PF(6)], a similar conversion yield was obtained (76.7+/-1.5%). AnFaeA was active in its free and immobilised form, with the latter retaining a part of its synthetic activity after 5 consecutive 24h-period reaction cycles. Sinapic acid was esterified to one of the primary hydroxyl groups of glycerol and retained, after esterification, 63.1+/-0.3% and 89.5+/-1.1% of its antioxidant activity against low-density lipoprotein oxidation, when added at concentrations of 10 and 60muM, respectively, in the assay mixture.     

Enzyme synthesis of oligosaccharides using cashew apple juice as substrate

The use of agriculture substrates in industrial biotechnological processes has been increasing because of their low cost. In this work, the use of clarified cashew apple juice was investigated as substrate for enzyme synthesis of prebiotic oligosaccharide. The results showed that cashew apple juice is a good source of reducing sugars and can be used as substrate for the production of dextransucrase by Leuconostoc citreum B-742 for the synthesis of oligosaccharides using the crude enzyme. Optimal oligosaccharide yield (approximately 80%) was obtained for sucrose concentrations lower than 60 g/L and reducing sugar concentrations higher than 100 g/L.