A kinetic study of immobilized lipase catalysing the synthesis of isoamyl acetate by transesterification in n-hexane.

Isoamyl acetate was synthesized by lipase-catalyzed transesterification of ethyl acetate in n-hexane. The selectivity and rates of ester formation decreased when water content of the immobilized enzyme exceeded 3% (w/w). Experimental observations clearly indicate that the substrates as well as the product (ethanol) act as dead-end inhibitors. A ping-pong bi-bi mechanism with competitive inhibition by substrates and products is proposed that predicts the experimental observation satisfactorily.     

Optimization and kinetic study of immobilized lipase-catalyzed synthesis of ethyl lactate

Abstract

Enzymatic synthesis of ethyl lactate catalyzed by immobilized lipase has been investigated. The reaction variables (including the molar ratio of ethanol to acid, total substrate amount, temperature, reaction time and rotation speed) were selected in accordance with the Plackett–Burman design and were further optimized via response surface methodology. The molar ratio of ethanol to acid, total substrate amount and reaction time were screened out as significant variables for the optimization study. A 20-run, full-factorial, central composite design was used to construct the statistical model and the optimal conditions obtained were as follows: molar ratio of ethanol to acid of 8.3:1, total substrate amount of 0.4 g, reaction time of 26.87 h with temperature of 55°C and rotation speed of 150 rpm. Under the optimal conditions, the yield of ethyl lactate was up to 24.32%; close to the 25.13% obtained using the commercial lipase, Novozym 435. Due to the low cost and simple immobilization process, the lipase prepared in the present work could have great potential in enzymatic applications. Additionally, a kinetic model with inhibition by both ethanol and lactic acid following a ping-pong bi-bi mechanism was proposed.     

Modelling and experimental studies on lipase-catalyzed isoamyl acetate synthesis in a microreactor

A lipase-catalyzed synthesis of isoamyl acetate was studied in a continuously operated pressure-driven microreactor. The esterification of isoamyl alcohol and acetic acid occurred at the interface between n-hexane and an aqueous phase with dissolved lipase B from Candida antarctica. By adjusting flow rates of both phases, a parallel laminar flow with liquid–liquid boundary in the middle of the microchannel could be reestablished and a separation of phases was achieved at the y-shaped exit of the microreactor. Since product remained in the organic phase, this also enabled its continuous separation from the aqueous phase with the enzyme. A three-dimensional mathematical model was developed, considering the velocity profile developed for steady-state conditions between two immiscible fluids. The model contained convection, diffusion, and enzyme reaction terms, where esterification rate was described with a Ping-Pong Bi-Bi mechanism and inhibition by both substrates. Experimental data, which were in good agreement with model simulations, have demonstrated 35% conversion at residence time 36.5 s at 45 °C and at 0.5 M acetic acid and isoamyl alcohol inlet concentrations, which is much faster as in any literature reported so far. According to model simulations, obtained by non-equidistant finite differences numerical solutions of complex non-linear equations system, further microreactor design and process optimization are feasible.     

Enzymatic synthesis of isoamyl acetate using immobilized lipase from Rhizomucor miehei

The effects of important reaction parameters for enhancing isoamyl acetate formation through lipase-catalyzed esterification of isoamyl alcohol were investigated in this study. Increase in substrate (acid) concentration led to decrease in conversions. A critical enzyme concentration of 3 g l(-1) was detected for a substrate concentration of 0.06 M (each of alcohol and acid). Solvents with partition coefficient higher than 1000 (log P>3.0) supported enzyme activity to give high conversions. Acetic acid at higher concentrations could not be esterified easily probably owing to its role in lowering the microaqueous pH of the enzyme. Extraneous water/buffer addition decreased the isoamyl acetate yields slightly ( approximately 10%) at 0.005-0.01% v/v of the reaction mixture and drastically (>40%) at above 0.01% v/v. Buffer saturation of the organic solvent employed improved esterification (upto two-fold), particularly at moderately higher substrate concentrations (>0.18 M). Employing acetic anhydride instead of acetic acid resulted in a two-fold increase in the yields (at 0.25 M substrate). Use of excess nucleophile (alcohol) concentration by increasing the alcohol/acid molar ratio resulted in higher conversions in shorter duration (upto eight-fold even at 1.5 M acetic acid). Yields above 80% were achieved with substrate concentrations as high as 1.5 M and more than 150 g l(-1) isoamyl acetate concentrations were obtained employing a relatively low enzyme concentration of 10 g l(-1). The operational stability of lipase was also observed to be reasonably high enabling ten reuses of the biocatalyst.     

Lipase-catalyzed synthesis of isoamyl butyrate. A kinetic study.

Kinetics of lipase-catalyzed esterification of butyric acid and isoamyl alcohol have been investigated. The reaction rate could be described in terms of the Michaelis-Menten equation with a Ping-Pong Bi-Bi mechanism and competitive inhibition by both the substrates. No evidence of any significant diffusional limitations was detected that could affect the kinetics. The values of the apparent kinetic parameters were computed as: V(max)=11.72 micromol/min/mg; K(M, Acid)=0.00303 M; K(M, Alcohol)=0.00306 M; K(i, Acid)=1.05 M; and K(i, Alcohol)=6.55 M. This study indicates a competitive enzyme inhibition by butyric acid during lipase-catalyzed esterification reaction. Butyric acid, being a short-chain polar acid, concentrates in the microaqueous layer and causes a pH drop in the enzyme microenvironment leading to enzyme inactivation. Butyric acid binds to acyl-enzyme complex unproductively to yield a dead-end intermediate that can no longer give rise to an ester. High concentration of butyric acid gave rise to inactivation of the biocatalyst in addition to dead-end inhibition.     

Optimization of isoamyl acetate production by using immobilized lipase from Mucor miehei by response surface methodology

Immobilized lipase from Mucor miehei was employed for the esterification of isoamyl alcohol with acetic acid in n-heptane solvent. The important process variables studied were enzyme/substrate (E/S) ratio, alcohol (acid) concentration, and incubation period. Based on Box-Behnken design of experiments, a second order response function was developed. The percentage esterification increased with both E/S ratio and time and decreased with alcohol (acid) concentration. The model indicated optimum conditions for maximum esterification ranging from 20 to 99.6% in the alcohol (acid) concentration range of 0.031 to 0.3 M for a range of E/S ratios 8.33 to 50 g/mol, which were in good agreement with the experimental yields.     

A kinetic study of lipase-catalyzed reversible kinetic resolution involving verification at miniplant-scale

Lipase-catalyzed kinetic resolution of racemates is a popular method for synthesis of chiral synthons. Most of these resolutions are reversible equilibrium limited reactions. For the first time, an extensive kinetic model is proposed for kinetic resolution reactions, which takes into account the full reversibility of the reaction, substrate inhibition by an acyl donor and an acyl acceptor as well as alternative substrate inhibition by each enantiomer. For this purpose, the reversible enantioselective transesterification of (R/S)-1-methoxy-2-propanol with ethyl acetate catalyzed by Candida antarctica lipase B (CAL-B) is investigated. The detailed model presented here is valid for a wide range of substrate and product concentrations. Following model discrimination and the application of Haldane equations to reduce the degree of freedom in parameter estimation, the 11 free parameters are successfully identified. All parameters are fitted to the complete data set simultaneously. Six types of independent initial rate studies provide a solid data basis for the model. The effect of changes in substrate and product concentration on reaction kinetics is discussed. The developed model is used for simulations to study the behavior of reaction kinetics in a fixed bed reactor. The typical plot of enantiomeric excess versus conversion of substrate and product is evaluated at various initial substrate mixtures. The model is validated by comparison with experimental results obtained with a fixed bed reactor, which is part of a fully automated state-of-the-art miniplant.     

Optimization of lipase-catalyzed synthesis of citronellyl acetate in solvent-free medium

Summary Citronellol esterification catalyzed byCandida antarctica lipase is performed with high yields (74%) in a solvent-free medium. The use of dessicants gives a 10% yield enhancement and substrate excess consumption by adding calculated amounts of acetic acid lead to a 80% pure citronellyl acetate. Quantities up to 100 ml are treated with success.     

Enhanced synthesis of isoamyl acetate using liquid-gas biphasic system by the transesterification reaction of isoamyl alcohol obtained from fusel oil

In this work, the transesterification reaction of isoamyl alcohol obtained from fusel oil and leading to the synthesis of isoamyl acetate was conducted simultaneously with in situ ethanol removal, which allows to shift the reaction equilibrium toward ester synthesis. The extracellular Aspergillus oryzae lipase was immobilized into calcium alginate. Effects of immobilization conditions on the loading efficiency and on the specific activity of entrapped lipase were investigated. The kinetic transfer of volatile reactants from the reactor was investigated using an experimentally first order kinetic model, in order to approve the feasibility of the liquid-gas system with continuous ethanol removal in the ester synthesis. The effects of the most influent parameters affecting the reaction have been also investigated using a Doehlert matrix design. The better operating conditions for isoamyl acetate synthesis were: a temperature of 68.5°C and a respective isoamyl alcohol and A. oryzae lipase concentration of 0.72 M and 2.39 g/L. At these conditions, the resulting reaction conversion and ethanol extraction yields were of 89.55 and 69.60%, respectively. The use of the fluidized bed reactor with continuous ethanol removal has allowed to improve the reaction conversion which was two times than the conversion higher obtained in batch reactor. Furthermore, under the optimized conditions in the fluidized bed reactor, the reaction conversion and the ethanol extraction yields were increased by 44.8 and 36.2%, respectively.     

Enhanced production of isoamyl alcohol and isoamyl acetate by ubiquitination-deficient Saccharomyces cerevisiae mutants

Aromatic compounds are an important element in the flavor of yeast-fermented alcohol. We isolated mutants of Saccharomyces cerevisiae capable of growth at high levels of hydrostatic pressure. Among them, the HPG1 mutants, with a defect in their Rsp5 ubiquitin ligase, were found to produce high amounts of aromatics due to enhanced leucine uptake, with isoamyl alcohol production 2- to 3-fold and isoamyl acetate production 4- to 8-fold that of the wild-type strain. The result suggests that the HPG1/RSP5 mutant alleles could be new resources for producing these flavoring compounds for yeast-fermented alcoholic beverages.     

Kinetics of lipase catalyzed isoamyl acetate synthesis at high hydrostatic pressure in hexane

Lipase-catalyzed synthesis of isoamyl acetate in hexane at 10–250 MPa at 80°C and 1–100 MPa at 40°C resulted in activation volumes of −12.9 ± 1.7 and −21.6 ± 2.9 cm³ mol⁻¹, respectively. Increasing pressure from 10 to 200 MPa resulted in approximately 10-fold increase in V _max at both 40 and 80°C. Pressure increased the K _m from 2.4 ± 0.004 to 38 ± 0.78 mM at 40°C. In contrast, at 80°C the pressure did not affect the K _m.     

Enzymatic synthesis of isoamyl butyrate using immobilized Rhizomucor miehei lipase in non-aqueous media

Isoamyl butyrate, an important fruity flavor ester, was synthesized using Rhizomucor miehei lipase immobilized on a weak anion exchange resin (Lipozyme IM-20) by the esterification of isoamyl alcohol and butyric acid. The effects of various reaction parameters such as substrate and enzyme concentrations, substrate molar ratio, temperature and incubation time have been investigated. Yields above 90% were obtained with substrate concentrations as high as 2.0 M. No evidence of enzyme inhibition by butyric acid was present up to 1.0 M concentration. Acid inhibition and, to a small extent, alcohol inhibition were evident above 1.0 M substrate concentration. Conversions reached a saturation value by the end of 24–48 h of incubation due to the accumulation of the water of reaction. The equilibrium was successfully pushed forward towards esterification by removing the accumulated water using a molecular sieve.Journal of Industrial Microbiology & Biotechnology (2000) 25, 147–154. Received 09 February 2000/ Accepted in revised form 24 June 2000     

Lipase-catalyzed synthesis of propyl-phenyl acetate: a kinetic and thermodynamic study

Bioprocess and Biosystems Engineering - This study focuses on the synthesis of propyl-phenyl acetate via esterification reaction in the presence of immobilized Candida antartica...     

Lipase-catalyzed synthesis of geranyl acetate in n-hexane with membrane-mediated water removal.

The esterification of geraniol with acetic acid in n-hexane was investigated. A commercial lipase preparation from Candida antarctica was used as catalyst. The equilibrium conversion (no water removal) was found to be 94% for the reaction of 0.1 M alcohol and 0.1 M acid in n-hexane at 30 degrees C. This was shown by both hydrolysis and esterification reactions. The activation energy of reaction over the temperature range 10 degrees to 50 degrees C was found to be 16 kJ/mol. The standard heat of reaction was -28 kJ/mol. Membrane pervaporation using a cellulose acetate/ceramic composite membrane was then employed for selective removal of water from the reaction mixture. The membrane was highly effective at removing water while retaining all reaction components. Negligible transport of the solvent n-hexane was observed. Water removal by pervaporation increased the reaction rate by approximately 150% and increased steady-state conversion to 100%.     

Wax ester synthesis by lipase-catalyzed esterification with fungal cells immobilized on cellulose biomass support particles

Esterification reactions between long-chain alcohol and oleic acid were performed for producing wax esters. The reaction can be catalyzed efficiently by cell-bound lipase of Rhizopus niveous fungal cells immobilized within cellulose biomass support particles. Carrying out the reaction in a solvent-free system is feasible by adding a molecular sieve for dehydration purposes. To optimize the yield, addition of a molecular sieve should be performed gradually during the whole course starting from the beginning of the reaction. The influence of reaction conditions such as temperature and substrate concentrations on reaction rates and yields were investigated; however, this reaction system is under the influence of both internal and external mass transfer resistance. Conducting the reaction in an organic solvent system with hexane or heptane as the solvent can eliminate diffusional effects. Reaction kinetics were subjected to detailed study in this system. The kinetics of the reaction can be represented satisfactorily by a Ping-Pong Bi Bi mechanism with deadend inhibition by alcohol.     

Kinetic study of the lipase-catalyzed synthesis of triolein

The kinetics of the synthesis of triolein catalyzed by immobilized Mucor miehei lipase were studied. Equilibrium constants for the synthesis of mono-, di-, and triolein were calculated from the equilibrium compositions for different initial ratios of glycerol and oleic acid by means of multiresponse regression. The 1,3-specific lipase can catalyze the synthesis of triolein because the ester enzymatically formed with the primary alcohol isomerizes, through acyl migration, to an ester on the secondary hydroxyl. The freed primary hydroxyl may then undergo further enzymatic conversion. The rates of isomerization depend on the concentration of oleic acid. (c) 1993 Wiley & Sons, Inc.     

Terpene ester synthesis by lipase-catalyzed transesterification

Summary Five lipases were screened for their ability to synthesize terpene esters by transesterification. The nature of terpene alcohol and enzyme, as well as the chain length of the acyl donor used affected the product yields. Lipase AY from Candida rugosa gave the best overall yield (96.2%). Geraniol and tributyrin were also found to be the best reactants.     

Improvement of enzymatic synthesis yields of flavour acetates: The example of the isoamyl acetate

Summary Isoamyl acetate synthesis was chosen as a model to improve flavour acetate yields by optimising the enzymatic reaction. Alcohol:acid molar ratio, temperature, water content and amount of enzyme effects were analyzed. The optimum values were respectively 4, 45°C, 0,1% (w/v) and 0,5 g. In these conditions, the synthesis yield reached 80 % after 24 h of reaction and was found 15 times greater than those already reported in the literature.     

Kinetics and optimization of lipase-catalyzed synthesis of rose fragrance 2-phenylethyl acetate through transesterification

Lipase from Candida rugosa was immobilized on a polyvinylidene fluoride membrane for synthesis of rose flavor ester, 2-phenylethyl acetate. Response surface methodology (RSM) was employed for kinetic modeling of process and prediction the yield. The RSM was used in practice for determining the kinetic models by fitting the initial rate dates based on the equations of ping-pong bi–bi and order bi–bi model. The maximum reaction rate and kinetic constants were matched with the order bi–bi model. The specificity constant of the immobilized lipase was 10-folds higher than the free form indicated the enzyme–substrate affinity, and catalytic ability was enhanced after immobilization. Moreover, the effects of reaction parameters on the yield were evaluated by RSM using a Box–Behnken experimental design. Based on a ridge max analysis, the maximum conversion was 95.33 ± 2.57% at 38.78 h, 35.85 °C, and substrate mole ratio of 3.65:1. Furthermore, the order bi–bi kinetic model was simulated successfully in a batch reaction. A good prediction existed between the RSM results and integrated equation was found.