Interesterification and synthesis by Candida cylindracea lipase in microemulsions

Unusual reactions of interesterification and synthesis catalyzed by Candida cylindracea lipase have been tested in reverse microemulsions. The microemulsions used are made of fatty acids or triglycerides, the enzyme dissolved in a very low water quantity, Brij 35 used as surfactant and an alcoholic cosurfactant. In such a system, fats and alcohols are both the substrates of the enzyme and the microemulsion components. Incidentally, non specific Candida cylindracea lipase does not catalyze interesterification of short chain triglycerides, revealing a specificity for the chain length. Interesterification reactions tested in the presence of a given water quantity but with varying water activities show that it is the water activity and not the water quantity which is a fundamental parameter of the system. The effect of the surfactant (Brij 35) on the interesterification reaction is studied. Heptyl-oleate synthesis catalyzed by non-specific lipase is obtained in microemulsions at a 98% yield. Synthesis of glycerol esters is also tested in monophasic medium and mono and diglycerides are obtained.     

Immobilization of lipase for effective interesterification of fats and oils in organic solvent

In order to investigate quantitatively the interesterification reaction, triolein and stearic acid were used as substrates and eight commercially available lipases were tested for their suitability for the reaction. Three fungal lipase preparations were found to be suitable. The hydrolytic activity of the commercial lipases was tested with olive oil, and it 2was noted that there was no correlation between their hydrolytic and interesterification activities. Among the lipases tested, Mucor miehei lipase was chosen for further study because of it high protein content and its relatively high hydrolytic and interesterification activities, both of which are required for effective interesterification. The effect of water activity of the interesterification reaction was investigated. interesterification activity was shown to be maximum at the water activity of 0.25. As the water activity of the lipase increased, hydrolysis of triglyceride was accelerated. At zero water activity, high conversion was achieved, although interesterification activity was relatively lower than that at the water activity of 0.25. A new and simple immobilization method was developed in order to render hydrophobicity to the lipase and hence to improve the interesterification activity of the lipase. The lipase was immobilized covalently with glutaraldehyde or with six alkyl chains as spacers onto Florisil (magnesium silicate, a inorganic matrix). Interesterification activity of the immobilized lipase with the hydrophobic spacers were increased against that of re lipase. The increase of activity was up to 8-fold that of the original activity of free lipase when the spacer was 7-aminoheptanoic acids. Relatively high stability of the immobilized lipase was shown in a continuous packed bed column reactor with a half-life of 97 days. (c) 1993 John Wiley & Sons, Inc.     

On the performance of a hollow-fiber bioreactor for acidolysis catalyzed by immobilized lipase

The present communication describes the chemical modification of anhydrous butterfat by interesterification with oleic acid catalyzed by a lipase of Mucor javanicus. Two reactor configurations were tested, a batch-stirred tank reactor containing suspended lipase and a batch-stirred tank reactor in combination with a hollow-fiber membrane module containing adsorbed lipase. The goal of this research was to assess the advantage of using a (hydrophobic) porous support to immobilize the lipase in attempts to engineer butterfat with increased levels of unsaturated fatty acid residues (oleic acid) at the expense of medium-to-long chain saturated fatty acids (myristic and palmitic acids). Reactions were carried out at 40 degrees C in the absence of solvent under controlled water activity, and were monitored by chromatographic assays for free fatty acids. The results obtained indicate that the rate of interesterification using the proposed reactor configuration is enhanced by a factor above 100 relative to that using suspended lipase, for the same protein mass basis. Although hydrolysis of butterfat occurred to some degree, the enzymatic process that uses the hollow-fiber reactor was technically superior to the stirred tank system. Copyright 1998 John Wiley & Sons, Inc.     

Interesterification of fats and oils by immobilized fungus at constant water concentration

The kinetics of enzymatic interesterification of oils and fats, using acetone-dried cells of Rhizopus chinensis immobilized on biomass support particles as a lipase catalyst, were investigated in batch operations at several constant water concentrations.Even under microaqueous (i.e., low-water-content) conditions, not only interesterification but also hydrolysis occured, and the water content in the reaction system decreased. The reaction rates of interesterification and hydrolysis at constant water concentrations were determined.For the reactions between olive oil and methyl stearate at several water concentrations, the parameters involved in the reaction model were determined by a trial-and-error method so as to make the calculated results correlate with the experimental data. The relationship between the parameters obtained and water concentration were examined.The rate constants involved in the reaction model of both interesterification and hydrolysis increased or decreased monotonically with the increasing water content, while the apparent activity of the lipase catalyst for interesterification had a maximum value at a water concentration of about 50 ppm. This suggests that when the water content is excessive the hydrolysis activity of lipase is accelerated more than its interesterification activity, and that when the water content is too little lipase activity can not be activated for either hydrolysis or interesterification.     

Kinetic modeling of interesterification reactions catalyzed by immobilized lipase

Kinetic data for lipase-catalyzed interesterification reactions between free fatty acids and triglycerides were collected and the dynamics of the interesterification reactions were successfully modeled using tow rate experssions requiring a total of five adjustable parameters. One rate expression describes the disappearance of the free fatty acid (octanoic or linolenic acid), and the second describes the rate of release of fatty acid residues from the triglycerides (olive oil or milkfat). This model is able to account for the effects of the concentration of all chemical species participating in interesterification throughout the entire reaction. When the data for both milkfat and olive oil were subjected to nonlinear regression analyses using the same mathematical model, the parameter estimates for both systems were comparable. In addition to reproducing the tendencies observed experimentally, simulations of the interesterification system under a variety of initial conditions provided insight into the effects of several reaction variables which could not be examined experimentally. Among the most significant findings of the simulation work are (1) there is a limit beyond which increasing the initial concentration of water produces no further increase in the initial rate of the interesterification reaction; (2) an increase in the initial concentration of lower glycerides produces a concomitant increase in the rate of the interesterification reaction; (3) the free fatty acids inhibit the rate of hydrolysis of the fatty acid residues of the triglycerides; (4) there is a limit beyond which increasing the initial concentration of triglycerides produces no significant increase in the rate of either the hydrolysis reaction or the interesterification reaction. (c) 1994 John Wiley & Sons, Inc.     

Chemoenzymatic Preparation of Optically Active Long-Chain 3-Hydroxyalkanoates

The synthesis of optically active 3-hydroxyalkanoates of varying chain length (C_lo, C₁₄ and C₁₈) was investigated using chemoenzymatic methods. While bakers' yeast mediated reduction of 3-oxoalkanoates gave (R)-3-hydroxyalkanoates (e.e. >80%, yield —10%), both enantiomers were obtained by enzymatic resolution of racemic methyl 3-butanoyloxyalkanoates using Geotrichum candidum lipase with moderate to good optical purity (e.e. 32–92%, yield 40–60% for both enantiomers). Lipase-catalysed interesterification, however, was found to proceed with similar enantioselectivity but with slow rate of conversion.     

Production of high-oleic acid tallow fractions using lipase-catalyzed directed interesterification, using both batch and continuous processing

Immobilized lipases were used to catalyze batch-directed interesterification of tallow, resulting in oleins containing significantly higher levels of unsaturated fatty acids than obtained by fractionation without lipase. After 14 days, a reaction catalyzed by 2% Novozym 435 yielded 57% olein unsaturation, compared with 45% in a no-enzyme control. Free fatty acid levels increased to 2-3% during reactions. Incubation of the enzyme in multiple batches of melted fat caused a gradual loss of interesterification activity, apparently due to progressive dehydration. The activity could be restored by addition of water to the reaction medium. Immobilized lipase was also used to catalyze directed interesterification in a continuous flow reactor. Melted tallow was circulated through a packed bed enzyme reactor and a separate crystallization vessel. The temperatures of the two parts of the apparatus were controlled separately to allow crystallization to occur separately from interesterification. Operation of the reactor with conventionally dry, prefractionated tallow allowed the formation of an olein consisting of up to 60% unsaturated fatty acids. The greatest changes in olein fatty acid composition were achieved when the fractionation temperature was kept constant at a value that promoted selective crystallization of trisaturated triglycerides that were continuously produced by enzymic interesterification. The enzyme could be reused without apparent loss of activity, and its activity was apparently enhanced by preincubation in melted tallow for up to several days. Control of both the water activity of the enzyme and tallow feedstock and of the absorption of atmospheric water vapor were required to maintain enzyme activity, during multiple reuse and minimize free fatty acid formation. This method may form the basis for a process to produce highly mono-unsaturated tallow fractions for use in food applications (e.g. frying) where a "healthy" low saturated fat product is required.     

Enzymatic interesterification of triglyceride with surfactant-coated lipase in organic media

Several surfactant-coated enzymes have been prepared by coating lipases of various origins with a nonionic surfactant, glutamic acid dioleylester ribitol (2C(18)Delta(9)GE). Enzymatic interesterification of tripalmitin with oleic acid using the surfactant-coated lipase was carried out in organic media. The surfactant-coated lipases could effectively catalyze the interesterification of glycerides better than did the powder lipases. A suitable organic solvent was an aliphatic hydrocarbon such as isooctane. The enzymatic activity for the interesterification strongly depended on the origin of the lipase. The surfactant-coated lipase prepared by Mucor javanicus showed the highest enzymatic activity for the interesterification of glycerides, although its powder lipase did not show enzymatic activity. Selective interesterification of glycerides could be performed by adjusting the concentration ratio of oleic acid to tripalmitin in isooctane. Di-substituted glyceride could be selectively produced when the concentration ratio of carboxylic acid to glycerides was 7. (c) 1995 John Wiley & Sons, Inc.     

Enzymic interesterification of fats: Laboratory and pilot-scale studies with immobilized lipase from Rhizopus arrhizus

An immobilized lipase suitable for fat interesterification has been prepared by precipitation with acetone of a commercial lipase from Rhizopus arrhizus onto diatomaceous earth. As observed previously with a less active enzyme from Aspergillus sp., the interesterification activity was enhanced by addition of purified lipase or by high loadings of commercial enzyme. The interesterification activities reached maximum values in both cases. For immobilized preparations with purified enzyme, interesterification activity was also enhanced by the presence of a precoat of glutaraldehyde cross-linked commercial lipase. A 2.9-L column of immobilized lipase was used to interesterify batches of shea oleine (67 kg) and shea oil (40 kg). Little activity was lost processing shea oleine, but slow poisoning of the bed occurred when shea oil was fed to the column.     

Enzymic interesterification of fats: The effect of non-lipase material on immobilized enzyme activity

An immobilized lipase (triacylglycerol acylhydrolase, EC 3.1.1.3) suitable for fat interesterification has been prepared by precipitation onto diatomaceous earth (Celite) with acetone of a crude lipase preparation from an Aspergillus. Non-lipase material present in the preparation which precipitated at high acetone concentrations or ovalbumin added prior to the immobilization reduced the measured interesterification activity without affecting lipolytic activity. The non-lipase material reduced the interesterification activity by as much as 50%. The interesterification activity of immobilized preparations was enhanced by the use of higher concentrations of the crude lipase or, more substantially, by admixture of purified lipase.     

Study on the kinetics of enzymatic interesterification of triglycerides for biodiesel production with methyl acetate as the acyl acceptor

A new route for biodiesel production using methyl acetate instead of methanol as the acyl acceptor was proposed in our previous research, and it has been found that this novel route could enhance the stability of the immobilized lipase greatly. In this paper, the kinetics of lipase-catalyzed interesterification of triglycerides for biodiesel production with methyl acetate as the acyl acceptor was further studied. First, a simplified model based on Ping Pong Bi Bi with substrate competitive inhibition mechanism was proposed to describe the reaction kinetics of the interesterification. During our further study, it was observed that three consecutive and reversible reactions occurred in the interesterification of triglycerides and methyl acetate. So, a kinetic model based on mass balance of three second-order reversible reactions was developed and the reaction rate constant, k, was determined by solving the differential rate equations of the reaction system. The results showed that k_DG–MG (0.1124) and k_MG–TA (0.1129) were much higher than k_TG–DG (0.0311), which indicated that the first step reaction was the limit step for the overall interesterification.     

Improving the application of microbial lipase by bio-imprinting at substrate-interfaces

Lipases have bio-imprinted with common substrate-interfaces and interesterification activities compared with amphiphile bio-imprinted counterparts. Bio-imprinting has yielded a 3.5- to 4.5-fold activity enhancement. Solvent-free medium was equally effective as hexane medium. Water addition erased the bio-imprinting effect. Bio-imprinting caused rate acceleration in the interesterification reaction and increased thermostability of the enzyme.     

Preparation of Triacylglycerol Molecular Species by Interesterification Using Endocellular Lipase in n-Hexane

The interesterification of triacylglycerol with fatty acid was done to prepare triacylglycerol molecular species. Optimum operating conditions for the interesterification using a 1,3-positional specific endocellular lipase from Rhizopus japonicus NR400 in a batch system were investigated. The reaction was done at 40°C for 5 hr in the following system: Trioleoylglycerol-palmitic acid = 1:3.5 (mol/mol), 10 ml n-hexane/g trioleoylglycerol, and 2500 units of enzyme/g trioleoylglycerol. Under these conditions, the content of palmitoyl groups in 1,3-positions of triacylglycerol was about 60 mol%. Additional interesterification (2-cycle reaction) using palmitic acid and the novel triacylglycerol prepared by one-step interesterification (1-cycle reaction) resulted in a preparation of highly pure 1,3-dipalmitoyl-2-oleoylglycerol.     

Interesterification selectivity in lipase catalyzed reactions of low molecular weight triglycerides

Summary In the absence of an organic solvent, a buffer to enzyme weight ratio of 1 gives maximum selectivity to interesterification over hydrolysis in a lipase-catalyzed mixture of triacetin and tributyrin. Addition of hexane enhances interesterification as does a reversed micelle configuration.     

Preparation of medium and long chain triacylglycerols by lipase-catalyzed interesterification in a solvent-free system

Synthesis of medium and long chain triacylglycerols (MLCTs) by lipase-catalyzed interesterification of soybean oil with medium chain triacylglycerols (MCTs) in a solvent-free system is investigated in this study. Firstly, reaction conditions of the interesterification were optimized. Under the optimum conditions (Lipozyme 435 of 8% as catalyst, substrate ratio of 40:60, heating temperature of 90 °C, reaction time of 6 h), MLCTs were obtained in a 74.9% yield Secondly, a two-step purification was conducted to reduce acid, peroxide values and diacylglycerol content to acceptable levels. After the deacidification by the neutralization and silica gel absorption, acid, peroxide values and diacylglycerol content were reduced to 0.14 mg/g, 1.5 mmol/kg and 1.2%, respectively. The determined levels of physicochemical parameters of purified MLCTs fell within the permitted ranges of the Chinese national standard specification for MLCTs. After a two-step purification, a qualified product was produced and can be used in pharmaceutical industry as a component of fat emulsion injection. The process for the preparation of MLCTs is scalable. Differently from previous studies, the aim of this study is to obtain MLCTs products meeting the national standard JX20070100 for structured triacylglycerols.     

Surfactant-Modified lipase for the catalysis of the interesterification of triglycerides and fatty acids

The lipase-catalyzed intresterification of triglycerides and fatty acids in n-hexane was studied. Initially, lipase Saiken was modified with a surfactant of sorbitan esters so that its dispersibility in hydrophobic organic media was improved. The surfactant-modified lipase formed in the modification process carried out in a buffer solution has 1,3-positional specificity and predominantly catalyzed the interesterification reaction in a microaqueous n-hexane system. The modification technique converted inactive lipases to very active biocatalysts for the interesterification of triglycerides and fatty acids. The pH and the weight ratio of surfactant to enzyme used during the lipase modification process have shown significant effects in determining the recoveries of the protein and enzyme activity from the buffer solution, the protein content of the modified lipase complex after being freeze dried, and the interesterification activity of the complex. The water content in the reaction solution has strongly influenced the enzyme activity as well as the distribution of the products. (c) 1995 John Wiley & Sons, Inc.     

Selective removal of linolenic acid from soybean oil by lipase-catalyzed interesterification at low temperature

Summary Linolenic acid, the component responsible for flavour instability of soybean oil could be reduced to 3% or less by interesterification (acidolysis) of the oil using lipases as catalysts at 10°C.     

Interesterification of phosphatidylcholine with lipases in organic media

Summary Lipases were investigated with respect to their ability to catalyse the incorporation of fatty acids into phosphatidylcholine (PC) by interesterification reactions. The enzymes were dried onto solid support materials and the conversions were carried out in water-saturated toluene. Three lipases (two fungal and one plant enzyme) had the desired activity; immobilized lipase from Mucor miehei (Lipozyme) was the most active enzyme. The Lipozyme-catalysed interesterification was selective for the sn-1 position of PC and during 48 h of reaction around 50% of the fatty acids in this position were replaced with heptadecanoic acid, a fatty acid which was practically absent in the original phospholipid. Due to adsorption on the support material and the competing hydrolysis reaction the total amount of PC in the reaction solution decreased to about 40% of the original amount. Higher interesterification rates were obtained with free fatty acids as acyl donors than with fatty acid esters. Offprint requests to: I. Svensson     

Continuous interesterification of oils and fats using dried fungus immobilized in biomass support particles

The industrial feasibility of an interesterification process using acetone-dried fungus (as a lipase catalyst) immobilized in biomass support particles (BSPs) was examined by continuous interesterification between olive oil and methyl stearate, where the water content of the reaction mixture (C_w) was controlled at a given value. The C_w affected not only the inactivation rate of lipase in the cells but also the production rate of the by-product (diglycerides). The optimal C_w was determined as about 100 ppm. The half-life of lipase in the cells was about 1200 h at the optimal C_w, suggesting that the interesterification process using the immobilized fungus is industrially feasible.     

Influence of Triacylglycerol Composition on the Emulsification Capacity of Oils

The emulsification capacity of several edible oils was determined in an aqueous system of bovine serum albumin. The relative emulsification capacity of corn, soybean, sesame, palm, palm kernel and coconut oils was 1.00, 0.99, 0.93, 0.90, 0.82 and 0.77, respectively. The emulsification capacity of straight mixed oils lay close to the mean value of that of the component oils. The capacity of mixed oils was decreased by 30～60% by interesterification. Monoacid triacylglycerols had a very low capacity in comparison with edible oils. By interesterification, the emulsification capacity of a mixture of trioleoylglycerol and trioctanoylglycerol was increased and approached the level of interesterified mixed edible oils.