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.     

Transesterification of divinyladipate with glucose at various temperatures by an alkaline protease of Streptomyces sp.

The transesterification of 1 M divinyladipate with 0.25 M glucose in dimethylformamide (DMF) catalyzed by 5 mg ml^–1 alkaline protease (24 units mg^–1 min^–1) from Streptomyces sp. gave 6-O-vinyladipoyl d-glucose as the main product with yields are between 60 and 90%. The optimum temperature for the reaction was about 50 °C.     

Modelling of Lipase Catalysed Transesterification Reactions

Transesterification of substituted ethanols with ethyl acetate is studied in the presence of two different lipases. The steric bulk of the substituent group plays a more important role than the electronic factors in the reaction. The reversible reaction is modelled mathematically, and the rate parameters in the model estimated by a transient parameter estimation procedure. The effect of lipase quantity, reaction temperature and substrate concentration on the reaction is studied independently. Product quantity exhibits a maxima for increasing substrate concentration which is modelled successfully with a substrate product inhibition model, and compared with the experimental data     

An Insight into the Active Site of Pseudomonas Fluorecens (P. cepacia) Lipase to Define the Stereochemical Demand for the Transesterification in Organic Solvents

The Pseudomonas fluorescens lipase-catalyzed transesterification of 2-methyl alkanols 1 and the 2-substituted oxiranemethanols 2 with vinyl acetate in organic solvents has been studied and the results discussed in terms of steric and electronic demand within the recently postulated models of the lipase active site.     

Effect of frying time on free fatty acid generation and esterification rate in Aspergillus sp.-catalyzed transesterification of cottonseed oil

Abstract

The present study was carried out to examine the effect of different frying times of edible oil on the extent of transesterification catalyzed by the whole-cell biocatalyst, Aspergillus (RBD01). Cottonseed oil was chosen as a conventional and cost-effective edible oil used commercially in India. The results showed that increased frying time of the oil decreased the extent of the transesterification reaction and hence alkyl ester production. Nearly complete (>98%) transesterification to ethyl alcohol was observed with used oil containing a free fatty acid (FFA) content of 3.7%, whereas beyond an FFA content of 4.0% the yield was reduced. Biocatalyzed hydrolysis (in the absence of the ethyl alcohol acceptor) of used frying oil resulted in decreasing yield of FFA from 84.0% to 27.6% with increasing frying time. With fried oil capable of a hydrolysis yield of 82–41% FFA, transesterification reactions were nearly complete. With the lower hydrolysis yields of 38–27% FFA, the transesterified ethyl ester yield decreased to 61–51%. These observations indicate that factors other than the presence of FFA and moisture influence the biocatalytic transesterification of used cooking oils.     

Transesterification with Candida Cylindracea Lipase in a Biphasic Aqueous-Organic System. Dependence of the Enantiomeric Ratio and the Reaction Rate on the Proportions of Water and Cyclohexane

18 September 1989

A transesterification reaction between 1-phenyl ethyl butyrate and 1-heptanol was carried out with Candida cylindracea lipase. The reaction was studied, with respect to the reaction rate and the enantiomeric ratio at different proportions of water and cyclohexane. A significantly lower reaction rate was observed for incubations with less than 0.5% water compared with those at a higher water content. Transesterification dominated over hydrolysis as the main reaction even at 70% water and a dramatic increase of the enantioselectivity was observed at this high water content. It is proposed that these effects depend on the mechanism of lipase catalysis at the interface of emulsion droplets. This interface binding gives 1-heptanol a positional preference compared with water for nucleophilic attack of the acyl enzyme and may, in addition, induce an optimal conformation for high enantioselectivity of the enzyme.     

Enzymatic Preparation of (R)-3-Hydroxy-2-Methylpropyl Butyrate by Asymmetric Hydrolysis

(R)-3-Hydroxy-2-methylpropyl butyrate was formed by asymmetric hydrolysis of the corresponding prochiral diester with lipase P (Amano) in high enantiomeric excess. Various physical and chemical reaction parameters were altered in order to optimize the stereoselectivity of the enzymatic reaction; low temperature (0d`C) combined with the application of salting-in salts or (polyhydric) alcohols turned out to be the most suitable systems providing the monobutyrate in 96% ee. Attempts towards chiral monobutyrate by enzymatic esterification of the corresponding prochiral diol were unsuccessful.     

New synthesis of artepillin C,a prenylated phenol,utilizing lipase-catalyzed regioselective deacetylation as the key step

We have synthesized artepillin C, a diprenylated p-hydroxycinnamate originally isolated from Brazilian propolis and exhibiting antioxidant and antitumor activities, from 2,6-diallylphenol. Replacement of the terminal vinyl with 2,2-dimethylvinyl group by olefin cross-metathesis and subsequent transformation yielded 2,6-diprenyl-1,4-hydroquinone diacetate. Candida antarctica lipase B-catalyzed deacetylation in 2-propanol regioselectively removed the less hindered acetyl group to give 2,6-diprenyl-1,4-hydroquinone 1-monoacetate. After triflation of the liberated 4-hydroxy group, a three-carbon side chain was introduced by palladium-mediated alkenylation with methyl acrylate. Final hydrolysis of the esters furnished artepillin C.     

Comprehensive semisyntheses of catathelasmols C,D, and E from D-glutamic acid,utilizing lipase-catalyzed site-selective reactions on intermediates

ABSTRACT

Catathelasmols C, D, and E, which had been isolated from Catathelasma imperiale as inhibitors for 11-hydroxysteroid dehydrogenases, were comprehensively semisynthesized from commercially available D-glutamic acid. The key synthetic intermediate, (R)-pentane-1,2,5-triol, was site-selectively acetylated by treatment with vinyl acetate and Candida antarctica lipase B (Novozym 435) in tetrahydrofuran (THF) at 25°C to furnish 1,5-diacetate (catathelasmol E, quantitative). The acetylation occurred site-selectively on the primary alcohols at the C-1 and C-5 positions over the secondary alcohol at the C-2 position. Dichromic acid oxidation provided 2-oxopentane-1,5-diyl diacetate (catathelasmol C, 78%). Burkholderia cepacia lipase-catalyzed transesterification with methanol in THF at – 5°C proceeded preferentially on the acetate at C-1 located adjacent to the C-2 carbonyl group over the other terminal acetate at the C-5 position. 5-Hydroxy-4-oxopentyl acetate (catathelasmol D) was obtained in 53% yield.