Kinetics of enzymatic synthesis of L-ascorbyl acetate by Lipozyme TLIM and Novozym 435

L-ascorbyl acetate was synthesized through lipase-catalyzed esterification using Lipozyme TLIM and Novozym 435. Four solvents, including methanol, ethanol, acetonitrile, and acetone were investigated for the reaction, and acetone and acetonitrile were found to be suitable reaction media. The influences of several parameters such as water activity (a _w), substrate molar ratio, enzyme loading, and reaction temperature on esterification of L-ascorbic acid were systematically and quantitatively analyzed. Through optimizing the reaction, lipase-catalyzed esterification of L-ascorbic acid gave a maximum conversion of 99%. The results from using Lipozyme TLIM and Novozym 435 as biocatalysts both showed that a _w was an important factor for the conversion of L-ascorbic acid. The effect of pH value on lipase-catalyzed L-ascorbic acid esterification in acetone was also investigated. Furthermore, results from a kinetic characterization of Lipozyme TLIM were compared with those for Novozym 435, and suggested that the maximum reaction rate for Lipozyme TLIM was greater than that for Novozym 435, while the enzyme affinity for substrate was greater for Novozym 436.     

Optimization of (R,S)-1-phenylethanol kinetic resolution over Candida antarctica lipase B in ionic liquids

The kinetic resolution of racemates constitutes one major route to manufacture optically pure compounds. The enzymatic kinetic resolution of (R,S)-1-phenylethanol over Candida antarctica lipase B (CALB) by using vinyl acetate as the acyl donor in the acylation reaction was chosen as model reaction. A systematic screening and optimization of the reaction parameters, such as enzyme, ionic liquid and substrates concentrations with respect to the final product concentration, were performed. The enantioselectivity of immobilized CALB commercial preparation, Novozym 435, was assayed in several ionic liquids as reaction media. In particular, three different ionic liquids: (i) 1-butyl-3-methylimidazolium hexafluorophosphate [bmim][PF₆], (ii) 1-butyl-3-methylimidazolium tetrafluoroborate [bmim][BF₄] and (iii) 1-ethyl-3-methylimidazolium triflimide [emim][NTf₂] were tested. At 6.6% (w/w) of Novozym 435, dispersed in 9.520 M of [bmim][PF₆] at 313.15 K, using an equimolar ratio of vinyl acetate/(R,S)-1-phenylethanol after 3 h of bioconversion, the highest possible conversion (50%) was reached with enantiomeric excess for substrate higher than 99%.     

Novel and highly effective chemoenzymatic synthesis of (2<Emphasis Type="Italic">R</Emphasis>)-2-[4-(4-cyano-2-fluorophenoxy)phenoxy]butylpropanoate based on lipase mediated transesterification

(2R)-2-[4-(4-Cyano-2-fluorophenoxy)phenoxy]butylpropanoate (cyhalofop-butyl, CyB) was synthesized by a chemoenzymatic route involving enantioselective transesterification with Candida antarctica lipase B (Novozym 435). The optimum organic solvent, acyl donor, a _w , reaction temperature and shaking rate for the transesterification were acetonitrile, n-butanol, 0.11, 45°C and 200 rpm, respectively. Under the optimum conditions, the maximum substrate conversion and the enantiomeric purity of the product were 96.9 and >99%, respectively. The total yield and enantiomeric purity of CyB by this chemoenzymatic synthesis were 60.4 and >99%, respectively; 15.3 and 21% higher than that of the traditional way (45 and 78%).     

Synthesis of methyl (R)-3-(4-fluorophenyl)glutarate via enzymatic desymmetrization of a prochiral diester

An efficient procedure for enzymatic desymmetrization of the prochiral dimethyl 3-(4-fluorophenyl)glutarate (3-DFG) in an aqueous–organic phase was successfully developed to prepare methyl (R)-3-(4-fluorophenyl)glutarate ((R)-3-MFG). Novozym 435 was selected as a highly efficient biocatalyst through lipase screening. The effects of various parameters in terms of co-solvent and its concentration, buffer pH, ionic strength and reaction temperature, on the reaction were investigated. It was found that 0.2 M phosphate buffer (pH 8.0) containing 20% MTBE (v/v) was the optimum reaction medium, and the optimum reaction temperature was 30 °C. Under the optimized reaction conditions, (R)-3-MFG was obtained in 95.6% ee value and 92.6% yield after 64 h when the concentration of 3-DFG and Novozym 435 were 200 mmol/l and 20 g/l respectively. Furthermore, Novozym 435 showed an excellent operational stability, retaining above 95% of the initial activity and enantioselectivity after 10 cycles of reaction. The developed method has a potential to be used for efficient enzymatic production of (R)-3-MFG.     

Assessment of two immobilized lipases activity and stability to low temperatures in organic solvents under ultrasound-assisted irradiation

Both stability and catalytic activity of two commercial immobilized lipases were investigated in the presence of different organic solvents in ultrasound-assisted system. In a general way, for Novozym 435, the use of ethanol as solvent led to a loss of activity of 35% after 10 h of contact. The use of iso-octane conducted to a gradual increase in lipase activity in relation to the contact time, reaching a maximum value of relative activity of 126%. For Lipozyme RM IM, after 5 h of exposure, the enzyme presented no residual activity when ethanol was used as solvent. The solvents tert-butanol and iso-octane showed an enhancement of about 20 and 17% in the enzyme activity in 6 h of exposure, respectively. Novozym 435 and Lipozyme IM presented high stability to storage after treatment under ultrasound-assisted system using n-hexane and tert-butanol as solvents.     

Microwave-assisted enzymatic resolution of (R,S)-2-octanol in ionic liquid

Combination use of microwave irradiation (MW) as heating mode and ionic liquid (IL) as reaction medium in enzymatic resolution of (R,S)-2-octanol with vinyl acetate as the acyl donor through transesterification by Novozym 435 was investigated. A synergistic effect of MW and IL [EMIM][NTf2], which was screened as the best reaction medium for this reaction, on improving enzyme activity and enantioselectivity was observed. The activity and enantioselectivity of Novozym 435 in [EMIM][NTf2] under MW were much higher than that in solvent free system under conventional heating, in solvent free system under MW, and in [EMIM][NTf2] under conventional heating, respectively. A systematic screening and optimization of the reaction parameters in [EMIM][NTf2] under MW were performed. Under the optimum conditions, 50% yield of (S)-2-octanol with 99% enantiomeric excess was obtained in 6 h. Furthermore, increased thermal stability and reusability of Novozym 435 under the combination use of MW and IL condition were also observed.     

Different enzyme requirements for the synthesis of biodiesel: Novozym 435 and Lipozyme TL IM

Enzymatic syntheses of biodiesel via alcoholysis of different vegetable oils (sunflower, borage, olive and soybean) have been studied. Loss of lipase activity induced by the nucleophile is greater with methanol than with ethanol, and is greater for Lipozyme TL IM than for Novozym 435. The optimum volume of ethanol depends on the loading of solid biocatalyst and is higher for preparations of Novozym 435 than for Lipozyme TL IM. Maximum rates were obtained with Lipozyme TL IM, for a molar ratio of alcohol to FA residues of 0.33. By contrast, Novozym 435 requires at least a 2:1 ratio. Alcoholysis of the vegetable oils is faster with Lipozyme TL IM than with Novozym 435. Use of a high loading of Novozym 435 (50% w/w) and a large molar excess of ethanol are required to obtain an initial rate similar to that obtained with Lipozyme TL IM at a lower enzyme loading (10% w/w) and an equimolar ratio of ethanol and FA residues. Novozym 435 produces quantitative conversions in only 7h at 25 degrees C, but complete conversions are not obtained with Lipozyme TL IM. Three stage stepwise addition of ethanol yields 84% conversion to ethyl esters for Lipozyme TL IM. Hence use of Novozym 435 is preferred. After nine cycles in a batch reactor Novozym 435 retained 85% of its initial activity.     

Water and water activity in the solid state fermentation of cassava starch by Aspergillus niger

Summary During the solid state fermentation (SSF) of cassava starch by Aspergillus niger estimations were made of total water, consumed water and the residual water remaining in small quantities after 23 h. A theoretical calculation based on the Ross equation showed that the water activity (a _w) of the substrate decreased to 0.85 towards the end of the culture. Such low values were assumed to be inhibitory to growth. The a _w of the substrate was increased when sugarcane bagasse was used as a high water retention capacity support. Higher growth rates and substrate conversion to biomass were obtained with this system, confirming that water availability is a critical factor in the SSF of starch substrates.Abbreviations A, B Experimental constants - a _w Water activity - H₂O_c Consumed water - H₂O_R Residual water - H₂O_T Total water - IDW Initial dry weight - IMC Initial moisture content - OUR Oxygen uptake rate - S Substrate dry weight - Sc Substrate conversion: consumed substrate/initial substrate - S _H Amount of sugars hydrolysed - SSF Solid state fermentation - X Biomass dry weight - W ^* Amount of solids/g of water     

Enzyme-facilitated synthesis of 1-nonene oxide and simple GC-MS SIM method for rapid screening of epoxidation processes

Abstract

Here, we describe an improved enzyme-facilitated epoxidation of 1-nonene using a conventional water bath shaker at ambient temperature. Enzymes were used to produce peroxy acids instantly from hydrogen peroxide (H₂O₂) and various perhydrolysis substrates. The peroxy acid generated was then utilised directly for in-situ oxidation of 1-nonene to 1-nonene oxide. Various parameters affecting the reaction were studied such as the nature of the peroxy acids, organic solvents, enzyme sources and enzyme concentrations. The highest conversion rate was achieved using phenylacetic acid as an oxygen carrier. 1-Nonene was converted most efficiently with 95% of the maximum yield by Novozym 435, an immobilised Candida antarctica lipase B, using dichloromethane as the reaction media. A minimum amount (16 mg, 1.4% w/w) of Novozym 435 was needed to maintain catalytic activity (160.0 Ug^?1). In addition, a simple and rapid Gas chromatography mass spectroscopy selective ion monitoring (GC-MS SIM) method was developed using a HP-5ms column for determining 1-nonene oxide. The method was found to be linear in the range of 29.9 to 298.8 mg/L with R² = 0.9981.     

Short communication: Effect of water activity on cell growth and phenol oxidase production by Streptomyces cyaneus var. viridochromogenes in surface culture

In surface cultures of Streptomyces cyaneus var. viridochromogenes, NaCl depressed water activity (a _w) without supporting growth. Reducing a _w from 0.987 to 0.951 led to 3- and 4-fold increases in intracellular and extracellular phenol oxidase activities, respectively.     

复合脂肪酶催化生物柴油的初步研究

初步探讨了复合脂肪酶催化生物柴油的工艺。优化了复合酶配比条件和叔丁醇反应体系。在无溶剂体系中,Novozym435分别与Lipozyme TLIM和Lipozyme RMIM均以70／30质量比混合时,甲酯得率分别达到94．52％和96．25％,比Novozym435单独催化时的甲酯得率分别提高了9．52％和9．99％。在叔丁醇体系中,当Novozym435与Li-pozyme TLIM和Lipozyme RMIM分别以60／40和80／20的质量比混合时,其甲酯得率分别为85．06％和81．5％,比Novozym435单独催化的效率分别提高了9．89％和7．48％。优化叔丁醇体系中复合酶催化条件后,甲酯得率达92％。     

Production of human milk fat substitutes enriched in omega-3 polyunsaturated fatty acids using immobilized commercial lipases and Candida parapsilosis lipase/acyltransferase

In human milk fat (HMF), palmitic acid (20–30%), the major saturated fatty acid, is mostly esterified at the sn-2 position of triacylglycerols, while unsaturated fatty acids are at the sn-1,3 positions, conversely to that occurring in vegetable oils.This study aims at the production of HMF substitutes by enzyme-catalyzed interesterification of tripalmitin with (i) oleic acid (system I) or (ii) omega-3 polyunsaturated fatty acids (omega-3 PUFA) (system II) in solvent-free media. Interesterification activity and batch operational stability of commercial immobilized lipases from Rhizomucor miehei (Lipozyme RM IM), Thermomyces lanuginosa (Lipozyme TL IM) and Candida antarctica (Novozym 435) from Novozymes, DK, and Candida parapsilosis lipase/acyltransferase immobilized on Accurel MP 1000 were evaluated. After 24-h reaction at 60 °C, molar incorporation of oleic acid was about 27% for all the commercial lipases tested and 9% with C. parapsilosis enzyme. Concerning omega-3 PUFA, the highest incorporations were observed with Novozym 435 (21.6%) and Lipozyme RM IM (20%), in contrast with C. parapsilosis enzyme (8.5%) and Lipozyme TL IM (8.2%). In system I, Lipozyme RM IM maintained its activity for 10 repeated 23-h batches while for Lipozyme TL IM, Novozym 435 and C. parapsilosis enzyme, linear (half-life time, t_1/2 = 154 h), series-type (t_1/2 = 253 h) and first-order (t_1/2 = 34.5 h) deactivations were respectively observed. In system II, Lipozyme RM IM showed linear deactivation (t_1/2 = 276 h), while Novozym 435 (t_1/2 = 322 h) and C. parapsilosis enzyme (t_1/2 = 127 h), presented series-type deactivation. Both activity and stability of the biocatalysts depended on the acyl donor used.     

Chemical Modification Causes Similar Change in Dependence on Water Activity of Chymotrypsin Hydration and Catalysis in Hexane

Amino groups in alpha-chymotrypsin were reacted with pyromellitic anhydride, introducing 17 to 32 additional carboxyl groups. This modification causes a major change in the water adsorption isotherm of the lyophilized protein powder. Little water is bound by the modified enzyme at water activity (a_w) below 0.35, but it shows increased water binding at a_w over 0.5. This correlates with a similar change in the a_w dependence of the catalytic activity of the enzyme powder suspended in hexane, with a much steeper increase in activity of the modified chymotrypsin.     

Increased xerotolerance of Saccharomyces cerevisiae during an osmotic pressure ramp over several generations

Although mechanisms involved in response of Saccharomyces cerevisiae to osmotic challenge are well described for low and sudden stresses, little is known about how cells respond to a gradual increase of the osmotic pressure (reduced water activity; a_w) over several generations as it could encounter during drying in nature or in food processes. Using glycerol as a stressor, we propagated S. cerevisiae through a ramp of the osmotic pressure (up to high molar concentrations to achieve testing-to-destruction) at the rate of 1.5 MPa day^-1 from 1.38 to 58.5 MPa (0.990–0.635 a_w). Cultivability (measured at 1.38 MPa and at the harvest osmotic pressure) and glucose consumption compared with the corresponding sudden stress showed that yeasts were able to grow until about 10.5 MPa (0.926 a_w) and to survive until about 58.5 MPa, whereas glucose consumption occurred until 13.5 MPa (about 0.915 a_w). Nevertheless, the ramp conferred an advantage since yeasts harvested at 10.5 and 34.5 MPa (0.778 a_w) showed a greater cultivability than glycerol-shocked cells after a subsequent shock at 200 MPa (0.234 a_w) for 2 days. FTIR analysis revealed structural changes in wall and proteins in the range 1.38–10.5 MPa, which would be likely to be involved in the resistance at extreme osmotic pressure.     

Conversion of a pentane-1,3,5-triol derivative using lipases as chiral catalysts and possible function of the lid for the regulation of substrate selectivity and enantioselectivity

Abstract

The enantioselective desymmetrization of a prochiral 3-O-silyl protected pentane-1,3,5-triol derivative was achieved by lipase-catalysed hydrolysis. The lipase from B. cepacia led to 95.4% enantiomeric excess (ee)of the (R)-configured compound (R)-4 at a theoretical yield of 79% and was isolated with 98.2% ee and 27% yield. Furthermore, it was found that the ee switched from an excess of (R)-4 to an excess of (S)-4 during the course of the reaction using crude lipase from C. rugosa under the same conditions. This finding was investigated in detail and compared to the change of substrate selectivity known for the lipase from M. miehei. It is supposed that both phenomena may result from a movement of the lid.     

Scale-up of the enantioselective reaction for the enzymatic resolution of (R,S)-ibuprofen

The reaction for the resolution of (R,S)-ibuprofen was scaled-up to yield gram quantities of (S)-ibuprofen. This was accomplished through two enantioselective reactions each catalysed by Novozym 435. In the first reaction, starting from 300 g of racemic ibuprofen, 88.9 g of enantioenriched (S)-ibuprofen with an enantiomeric excess of the order of 85% were produced. In the subsequent reaction, 75 g of the 85 % e.e. material were utilized to produce 38.4 g of (S)-ibuprofen with an enantiomeric excess of 97.5 %.     

Comparison of differently modified Pseudomonascepacia lipases in enantioselective preparation of a chiral alcohol for agrochemical use

Three methods for enzyme modification/immobilization were compared to enhance the catalytic performance of a commercially available lipase, Lipase PS from Pseudomonascepacia, in highly enantioselective transesterification of an agrochemically useful sec-alcohol, (R,?S)-HMPC [=(R,?S)-4-hydroxy-3-methyl-2-(2′-propenyl)-2-cyclopenten-1-one], with vinyl acetate as both acyl donor and reaction medium. The stearic acid-coated lipase showed the highest catalytic activity, with a specific activity improved by 54 times over the native lipase. The microcrystal salt-supported lipase and celite-adsorbed lipase also displayed much better performance as compared with the native lipase. All the three modified lipase preparations showed a similar thermal stability to that of the native enzyme. The enantioselectivity (E-value) was also quite satisfactory in all the cases (E>100 at 30°C), though a trend of slight decline was also observed with the temperature increase in the range of 25–60°C. The optimum aqueous pH, from which the modified lipases were prepared, was 6.0–7.0. A low water activity (a_w) of ca. 0.1 was favorable for all the three modified lipases. The stearic acid-coated lipase displayed prominent advantages in catalyzing the transesterification reaction at a very high (R,?S)-HMPC concentration up to 1.0?M.     

Evaluation of enantioselectivity in lipase-catalyzed acylation of hydroxyalkylphosphine oxides

The lipase-catalyzed optical resolution of 2-, 3-, and 5-hydroxyalkyl phosphorus compounds 1 provided the corresponding optically pure diastereomers in good yields. (S_P, R)- and (R_P, S)-1 were acylated faster than (S_P, S)- and (R_P, R)-1. The stereoselectivity at the phosphorus atom changed with the flexibility of the active sites in the lipases. The stereoselectivity at the phosphorus atom was higher in the reaction of 1a than in the reaction of 1b,c. The reaction rate of -hydroxyalkylphosphine oxide 1c was faster than that of 1a, although less enantioselectivity was observed at the phosphorus atom.     

Impact of some environmental factors on growth and production of ochratoxin A of/by <Emphasis Type="Italic">Aspergillus tubingensis,A. niger</Emphasis>, and <Emphasis Type="Italic">A. carbonarius</Emphasis> isolated from moroccan grapes

The effects of temperature, water activity (a_w), incubation time, and their combinations on radial growth and ochratoxin A (OTA) production of/by eight Aspergillus niger aggregate strains (six A. tubingensis and two A. niger) and four A. carbonarius isolated from Moroccan grapes were studied. Optimal conditions for the growth of most studied strains were shown to be at 25°C and 0.95 a_w. No growth was observed at 10°C regardless of the water activity and isolates. The optimal temperature for OTA production was in the range of 25°C∼30°C for A. carbonarius and 30°C∼37°C for A. niger aggregate. The optimal a_w for toxin production was 0.95∼0.99 for A. carbonarius and 0.90∼0.95 for A. niger aggregate. Mean OTA concentration produced by all the isolates of A. niger aggregate tested at all sampling times shows that maximum amount of OTA (0.24 μg/g) was produced at 37°C and 0.90 a_w. However, for A. carbonarius, mean maximum amounts of OTA (0.22 μg/g) were observed at 25°C and 0.99 a_w. Analysis of variance showed that the effects of all single factors (a_w, isolate, temperature and incubation time) and their interactions on growth and OTA production were highly significant.