Lipase catalyzed synthesis of cinnamyl acetate via transesterification in non-aqueous medium

Cinnamyl acetate is used as flavor and fragrance ingredient in food and cosmetic industries. This work focuses on the synthesis of cinnamyl acetate via lipase catalyzed transesterification of cinnamyl alcohol with vinyl acetate in non-aqueous medium. Among the different immobilized lipases employed, Novozym 435 was found to be the best catalyst in toluene as solvent. The effects of various parameters were studied systematically. With a mole ratio of 1:2 of cinnamyl alcohol to vinyl acetate and 10 mg catalyst, 96% conversion was obtained in 1 h at 40 °C. The ternary complex mechanism with inhibition by cinnamyl alcohol was found to fit the data well. The kinetics of the reaction was studied by using non-linear regression analysis. Enzymatic synthesis of cinnamyl acetate is an efficient process vis-à-vis chemical catalysis.     

Utilization of deep‐sea microbial esterase PHE21 to generate chiral sec‐butyl acetate through kinetic resolutions

We previously identified and characterized 1 novel deep‐sea microbial esterase PHE21 and used PHE21 as a green biocatalyst to generate chiral ethyl (S)‐3‐hydroxybutyrate, 1 key chiral chemical, with high enantiomeric excess and yield through kinetic resolution. Herein, we further explored the potential of esterase PHE21 in the enantioselective preparation of secondary butanol, which was hard to be resolved by lipases/esterases. Despite the fact that chiral secondary butanols and their ester derivatives were hard to prepare, esterase PHE21 was used as a green biocatalyst in the generation of (S)‐sec‐butyl acetate through hydrolytic reactions and the enantiomeric excess, and the conversion of (S)‐sec‐butyl acetate reached 98% and 52%, respectively, after process optimization. Esterase PHE21 was also used to generate (R)‐sec‐butyl acetate through asymmetric transesterification reactions, and the enantiomeric excess and conversion of (R)‐sec‐butyl acetate reached 64% and 43%, respectively, after process optimization. Deep‐sea microbial esterase PHE21 was characterized to be a useful biocatalyst in the kinetic resolution of secondary butanol and other valuable chiral secondary alcohols.     

Kinetics of cutinase catalyzed transesterification in AOT reversed micelles: modeling of a batch stirred tank reactor

A transesterification process is analyzed in its multiple kinetic components that include the determination of the kinetic constants for both substrates, butyl acetate (BAc) and hexanol (H), involved in the alcoholysis reaction and for the products formed (hexyl acetate (HAc) and butanol (B)), participating into the reverse reaction. The order of magnitude of these constants is discussed in relation with the AOT/isooctane reverse micellar system under study. The values of the equilibrium conversion (X(e)) and constant (K(eq)) were also determined. Diffusional limitations were detected for H concentrations lower than 450 mM and the correspondent effectiveness factors were calculated. Above 450 mM H the reaction is kinetically controlled. The operation of a batch stirred tank reactor (BSTR) was modeled considering the integrated rate equation for reversible kinetics.     

Evaluation of different approaches for lipase catalysed synthesis of citronellyl acetate

Three different approaches for lipase catalysed synthesis of citronellyl acetate by a commercial available immobilized lipase have been studied: a) direct esterification reaction of citronellol with acetic acid; b) alcoholysis of butyl acetate with citronellol and c) transesterification of citronellyl butyrate with butylacetate. Heptane was used as solvent for all the experiments. The extent of reaction occurred in the order alcoholysis>transesterification>esterification. Substrate partitioning between the immobilization support and the organic medium seems to greatly influence the catalytic performance of this enzyme preparation. Production of citronellyl acetate, was found to be dependent on the partition coefficient of the acyl donor which account the greatest value for the acetic acid.     

Study of the processes of butyl acetate regeneration from butanol-butyl acetate solutions by etherification of butanol with acetic anhydride (for use in production of penicillins]

Etherification of butanol by acetic anhydride in butanol-butyl acetate mixtures containing 0.09 to 3 per cent water was investigated. A method for processing the butanol-butyl acetate mixtures with the weight part of butanol up to 16 per cent by etherification of the latter with acetic anhydride was developed, the yield being 96 to 97 per cent and the weight part being at least 97.5 per cent. On the basis of the estimate of the raw material use for regeneration of butyl acetate from the butanol-butyl acetate solutions by etherification of butanol with acetic anhydride, the technical and economic advantages of the processing of such solutions by the described method were shown.     

Evaluation of a high surface area fractional precipitation process for the purification of paclitaxel from Taxus chinensis

In this study, we evaluated a high surface area fractional precipitation process to achieve the effective purification of paclitaxel, an anticancer agent, from plant cell cultures. Fractional precipitation experiments were performed by increasing the surface area per working volume (S/V) to 0.428/mm using a variety of ion exchange resins. When the cation exchange resin Amberlite IR 120 H was used, the highest purity (>85%) and yield (>80%) of paclitaxel could be obtained in the shortest fractional precipitation time (within 6 h). Use of an ion exchange resin resulted in the production of smaller paclitaxel precipitates since it inhibited the growth of particles. When Amberlite IR 120 H in particular was used, paclitaxel particles were 2 ?? 3 times smaller (less than 30 ??m radius) than those obtained in the absence of ion exchange resin. Paclitaxel particle size was inversely correlated with the zeta potential of the fractional precipitation solution after the addition of ion exchange resin.     

Catalytic properties of lipase adsorbed on nanocarbon-containing mesoporous silica in esterification and transesterification reactions

Nanocarbon-containing mesoporous silica covered with a varying amounts of nanostructured carbon of different morphologies were used as supports to immobilize Thermomyces lanuginosus lipase. The catalytic properties of the prepared biocatalysts were studied in both the transesterification of vegetable (linseed) oil in the presence of ethyl acetate and the esterification of the fatty acid (capric C10:0) in the presence of secondary (isopropyl or isoamyl) alcohols. The physico-chemical characteristics, such as the amount of adsorbed lipase, its specific activity, and the dependence of the activity and stability of the prepared biocatalysts on the support type were evaluated. The Michaelis-Menten kinetics was studied in the esterification of capric acid with isoamyl alcohol. The prepared biocatalysts were shown to retain up to 90% activity for >1000 h in the synthesis of isoamyl caprate. The half-time of the biocatalysts inactivation in the transesterification of linseed oil was found to be more than 700 h at 40°C.     

Development of a micelle-fractional precipitation hybrid process for the pre-purification of paclitaxel from plant cell cultures

A micelle-fractional precipitation hybrid process was developed for the effective pre-purification of the anticancer agent paclitaxel extracted from plant cell cultures. First, it was found that the efficiency of such a developed process could be remarkably enhanced by removing waxy substances originating from plant cells using the adsorbent sylopute. Paclitaxel yield was improved and the fractional precipitation time was shortened by increasing the surface area per working volume (S/V) of the reacting solution through the addition of a cation exchange resin (Amberlite IR120 or Amberlite 200), an anion exchange resin (Amberlite IRA400 or Amberlite IRA96), or glass beads. Most of the paclitaxel (>98%) could be obtained after about 12 h of fractional precipitation using Amberlite 200. Purity increased with increasing fractional precipitation time up to 9 h to about 85%, after which it showed little change. On the other hand, no paclitaxel precipitate was formed using either of the nonionic exchange resins because paclitaxel, which is hydrophobic, was strongly adsorbed on the hydrophobic resin surface. Since high-purity paclitaxel can be obtained in high yield and the precipitation time can be reduced by combining micelle formation with fractional precipitation, this hybrid method is expected to significantly enhance the final purification process.     

Influence of vegetable oils fatty-acid composition on biodiesel optimization

Biodiesel is an alternative fuel for diesel engines produced through transesterification of oleaginous feedstocks. To analyze the influence of the fatty-acid composition on biodiesel optimization, transesterification of several vegetable oils has been studied. Reactions were carried out in flasks filled with vegetable oils, heated to the reaction temperature and stirred at 1100 rpm. The reactions started when the methanol and potassium hydroxide solutions were added to the flasks. Concentration of catalyst, amount of methanol, reaction temperature and time were optimized using a factorial design and a surface response design. Also, a kinetics study was carried out to optimize the reaction time. Results showed that reaction parameters optimal values depend on the oil chemical and physical properties. It can be concluded from this field trial that the effect of both catalyst concentration and reaction time over the transesterification yield is greatly influenced by the saturation degree and fatty-acid chain length.     

Immobilization of lipase from Candida cylindraceae and its use in the synthesis of menthol esters by transesterification.

Lipase (EC 3.1.1.3) from Candida cylindraceae has been immobilized by the cellulose-titanium chloride method, and on EP-400 polyethylene, with and without glutaraldehyde crosslinking, to give active preparations when assessed by their ability to catalyse the hydrolysis of tributyrin. In both cases, the use of glutaraldehyde crosslinking was shown to improve the stability of the preparations for repeated use. The lipase immobilized on EP-400 polyethylene was found to be effective in transesterification using tributyrin or triacetin as acyl donors with l-menthol as acceptor. The production of methyl butanoate and of methyl acetate using this immobilized preparation was in each case enhanced in the presence of Amberlite IR 47 Anion exchange resin (OH form).     

Uptake and activation of acetate and butyrate in Clostridium acetobutylicum

Summary The pathway for uptake of acids during the solvent formation phase of an acetone-butanol fermentation by Clostridium acetobutylicum ATCC 824 was studied. ¹³C NMR investigations on actively metabolizing cells showed that butyrate can be taken up from the medium and quantitatively converted to butanol without accumulation of intermediates. The activities of acetate phosphotransacetylase, acetate kinase and phosphate butyryltransferase rapidly decreased to very low levels when the organism began to form solvents. This indicates that the uptake of acids does not occur via a reversal of these acid forming enzymes. No short-chain acyl-CoA synthetase activity or butyryl phosphate reducing activity could be detected. Based on our results and a critical analysis of literature data on acetone-butanol fermentations, it is suggested that an acetoacetyl-CoA: acetate (butyrate) CoA-transferase is solely responsible for uptake and activation of acetate and butyrate in C. acetobutylicum. The transferase exhibits a broad carboxylic acid specificity. The key enzyme in the uptake is acetoacetate decarboxylase, which is induced late in the fermentation and pulls the transferase reaction towards formation of acetoacetate. The major implication is that it is not feasible to obtain a batch-wise butanol fermentation without acetone formation and retention of a good yield of butanol.     

Absorption spectrum of admixtures coloring butyl acetate extract

Colour of butyl acetate extract (BAE) at the clarification stage in chemical purification of benzylpenicillin is one of the important qualitative parameters necessary for the process control. BAE is benzylpenicillin-enriched butyl acetate with colouring pigments and admixtures of unknown nature. The routine laboratory photocolorimetric method provides only periodical control. It is labour-consuming and does not enable determination of the process end. The specific characteristics of the butyl acetate extracts and their components in UV and visible spectra were studied and the absorption region of the admixtures (350-500 nm) colouring the extract with a maximum at 390 +/- 10 nm was determined. A photometric method, a definite wave length and analyzer Luch-II are recommended for optimal control of the clarification process. The apparatus was tested under laboratory conditions.     

Enzymatic synthesis of ethyl glucoside lactate in non-aqueous system

Ethyl glucoside lactate, a novel α-hydroxy acid derivative, was synthesized by transesterification in non-aqueous phase using immobilized lipase as biocatalyst. Parameters such as solvent type, substrate concentration, reaction temperature, and enzyme concentration were investigated to optimize the lipase-catalyzed transesterification. In solvent-free system with butyl lactate as both acyl donor and solvent, a 71% conversion was achieved. In order to investigate the effect of initial water content, the reactions were carried out in the mediums treated with molecular sieves. The results showed that conversion and initial rate decreased with the increase of water content. The conversion and initial rate reached to 95% and 67.4 mM/h, respectively, by carrying out the reaction under reduced pressure, which was employed to eliminate butanol and the initial water.     

Triphasic esterification of butanol and butyric acid in fermentation media

Butanol and butyric acid produced from acetone-butanol-ethanol (ABE) fermentation can be used to produce butyl butyrate, an important fragrance ester. However, low levels of butanol and butyric acid need to be purified from culture media first with energy-intensive distillation processes. In this study, a triphasic (organic/aqueous/fluorous) system is developed to esterify butanol and butyric acid in spent culture media into butyl butyrate directly without purification. The produced butyl butyrate forms a distinct organic phase floating on top and can then be separated easily. In a model system containing 37.1 g/L of butanol and 44.1 g/L of butyric acid, 57% of the butanol is converted to butyl butyrate after 8 h of esterification. With multiple cycles of esterification and product removal, butanol conversion can be further increased to 86%. When spent culture medium containing 7.12 g/L of butanol and 4.81 g/L of butyric acid is used for esterification, 38% of butanol (0.36 mmol) is consumed and 0.33 mmol of butyl butyrate is produced. However, when ABE fermentation and esterification are carried out simultaneously, only 0.042 mmol of butyl butyrate is produced, probably due to the incompatible pH requirements for cell growth (pH 5–7) and esterification (pH 2–3).     

Continous ethyl acetate production by Kluyveromyces fragilis on whey permeate

The synthesis of ethyl acetate by Kluyveromyces fragilis on diluted whey permeate was studied. Ethanol, lactose and O₂ are the direct precursors for ethyl acetate synthesis by this yeast. Ethyl acetate production is affected by many parameters, particularly the carbon/nitrogen (C/N) ratio, Tween 80 and iron. Ethyl acetate synthesis is optimum for C/N = 45. Tween 80 lowered slightly the level of ethyl acetate whereas iron completely stopped ethyl acetate production. The level of ethanol in the feed, the dissolved O₂ (DO) and dilution rate (D) were also optimised. Thus at D = 0.24 h ^–1, for 4 g/l of ethanol in the feed and 40% DO, the productivity of ethyl acetate was optimal (0.7 g/l per hour). Correspondence to: A. Miclo     

One‐pot synthesis of (R)‐1‐(pyridin‐4‐yl)ethyl acetate using tandem catalyst prepared by co‐immobilization of palladium and lipase on mesoporous foam: Optimization and kinetic modeling

The synthesis of (R )‐1‐(pyridin‐4‐yl)ethyl acetate was achieved over tandem palladium‐lipase catalyst with 100% selectivity using 4‐acetyl pyridine as a reactant. The 2% w /w palladium and lipase catalyst was successfully co‐immobilized in the microenvironment of the mesocellular foam and characterized by various techniques. The palladium metal from catalyst hydrogenated 4‐acetyl pyridine to form 1‐(pyridin‐4‐yl)ethanol. The generated intermediate product then underwent kinetic resolution over lipase and selectively gave (R )‐1‐(pyridin‐4‐ yl)ethyl acetate. The catalytic conditions were then studied for optimal performance of both steps. The reaction conditions were optimized to 50 °C and toluene as a solvent. Both chemical and enzymatic kinetic models of the reaction were developed for a given set of reaction conditions and kinetic parameters were predicted. At optimal conditions, the obtained selectivity of intermediate (1‐(pyridin‐4‐yl)ethanol) was 51.38%. The final product yield of ((R )‐1‐(pyridin‐4‐yl)ethyl acetate) was 48.62%.     

Kinetic modeling of immobilized-lipase catalyzed transesterification of n-octanol with vinyl acetate in non-aqueous media

Organic esters are employed as solvents, fragrance, flavors, and precursors in a variety of industries. Particularly, aliphatic esters are greatly used in flavor industry, mainly as fixatives and modifiers, and aromatic esters in fragrance compositions. Esters are produced by a variety of methods among which esterification and transesterification with acid catalysts under reflux conditions are prominent. The use of biocatalysts provides an opportunity for carrying out reactions under milder conditions leading to better quality products suitable in fragrance and flavor industry. Transesterification of n-octanol with vinyl acetate was studied at 30 °C as a model reaction by employing different lipases as catalysts such as Psedomonas species lipase immobilized on diatomite, free Candida rugosa lipase. Novozym 435 (lipase B from Candida antarctica; immobilized on macro-porous polyacrylic resin beads) and Lipozyme IM 20 (Mucor miehei lipase immobilized on anionic resin). Novozym 435 was found to be the most active catalyst in heptane as a solvent. A conversion of 82% with 100% selectivity of n-octyl acetate was obtained at 30 °C in 90 min using equimolar quantities of the reactants with 0.833 g l⁻¹ of Novozym 435. Transesterification of other alcohols such as n-decanol, benzyl alcohol, cinnamyl alcohol, 2-ethyl-1-hexanol, 1-phenyl ethyl alcohol, and 2-phenyl ethyl alcohol was also studied with vinyl acetate. The analysis of the initial rate data and progress curve data showed that the reaction obeys the ternary complex bi–bi mechanism with inhibition by n-octanol. The experimental and theoretical values matched very well.

The order of transesterification reactivity of vinyl acetate with various alcohols in presence of Novozym 435 under otherwise identical conditions at 30 °C was found to be as follows:

n-octanol>n-decanol>benzylalcohol>cinnamylalcohol>2-ethyl-1-hexanol>2-phenylethylalcohol>1-phenylethylalcohol.

     

Transesterification of palm oil to methyl ester on activated carbon supported calcium oxide catalyst

In this study, methyl ester (ME) was produced by transesterification of palm oil (CPO) (cooking grade) using activated carbon supported calcium oxide as a solid base catalyst (CaO/AC). Response surface methodology (RSM) based on central composite design (CCD) was used to optimize the effect of reaction time, molar ratio of methanol to oil, reaction temperature and catalyst amount on the transesterification process. The optimum condition for CPO transesterification to methyl ester was obtained at 5.5 wt.% catalyst amount, 190 °C temperature, 15:1 methanol to oil molar ratio and 1 h 21 min reaction time. At the optimum condition, the ME content was 80.98%, which is well within the predicted value of the model. Catalyst regeneration studies indicate that the catalyst performance is sustained after two cycles.     

Analysis of tyrosine and deuterium labelled tyrosine in tissues and body fluids

A gas chromatographic mass spectrometric method has been developed to determine tyrosine and deuterium labelled tyrosine in biological samples using alpha-methyltyrosine (alpha-Me Ty) or m-hydroxyphenylalanine as internal standards. With the latter standard both labelled and unlabelled tyrosine as well as alpha-Me Ty can be determined simultaneously, in for example human blood, following administration of alpha-Me Ty to inhibit catecholamine synthesis. After isolation of the amino acids on an ion exchange column (Amberlite IR 120) the butyl ester pentafluoropropionyl derivatives were prepared. In human plasma the precision of the method was determined at a level of 80 nmol tyrosine ml-1 and found to be +/- 5% (coefficient of variation, n = 10).