Orlistat-induced molecular bio-imprinting of microbial lipase

Some microbial lipases bio-imprinted with the reversible lipase inhibitor, Orlistat. Comparison of interesterification activities indicated that Orlistat bio-imprinting is equally effective as amphiphile imprinting and yields a 3.5–4.0-fold activity enhancement. Solvent-free incubation medium was as effective as hexane medium. Water addition into the incubation medium erased the bio-imprinting effect; hence, lid opening should be the mechanism of activation. This study provides additional proof to the hypothesis that lipase bio-imprinting is an active-site related phenomenon.     

脂肪酶生物印迹研究进展

脂肪酶是一种广泛应用的水解酶。生物印迹技术是一项新兴技术,它使脂肪酶在有机溶剂中发挥更好的催化能力,如更高的活性和稳定性,从而扩大了脂肪酶作为生物催化剂在工业上的应用。本文介绍了脂肪酶蛋白质的结构特点,脂肪酶生物印迹的过程和原理,对生物印迹过程中印迹模板的种类和选择原则、保护剂的作用等主要影响因素进行了讨论,并对不同种类脂肪酶的生物印迹条件和适用的反应及生物印迹效果作了归纳总结,指出了目前脂肪酶生物印迹技术存在的问题和发展前景。     

Bio-imprinting of microbial lipase at air–water interface

Bio-imprinting has been introduced as a technique of interfacial activation of lipase for anhydrous reaction applications. In this study, air–water (bubble) interfaces were compared to amphiphile and substrate interfaces in microbial lipase bio-imprinting. Results indicated that the bubble interface is equally effective on lipase interesterification activity and produces a 4–4.5-fold increase compared with the enzymes as supplied. Interesterification activity can be explained in terms of effects upon the accessibility of the lipase active site. This technique provides an easier, cheaper and product-friendly way of lipase bio-imprinting.     

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.     

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.     

Enhancement of transesterification-catalyzing capability of bio-imprinted tannase in organic solvents by cryogenic protection and immobilization

Improvement of transesterification-catalyzing capability of bio-imprinted tannase is a crucial question of whether to be efficiently utilized in organic media. As for biotransformation of tannic acid to propyl gallate, bio-imprinting technique can dramatically enhance the transesterification-catalyzing capability of tannase. In this work, both cryogenic protection and immobilization were utilized to further improve its apparent catalytic capability in organic media. The results show that Triton-X-100, mannose, and magnesium ion all have a positive effect on cryogenic protection of the tannase. Particularly, combinational application of the three cryoprotectants increases its catalytic performance by 2.7-fold factor. Also, immobilization further elevates its catalytic capability by 2.1 folds. Noteworthily, the coupling application of immobilization and cryo-protection can cause the conversion rate of substrate of the bio-imprinted tannase to increase to a promising 70%. Consequently, it will be helpful to fully utilize tannase in organic phase.     

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.     

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.     

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.     

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.     

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.     

Effect of moisture on enzymatic reaction in supercritical carbon dioxide

The continuous acidolysis of triolein and stearic acid was carried out by an immobilized lipase to elucidate the characteristics of supercritical carbon dioxide (SC-CO₂) as a reaction medium. At first, an effect of temperature and pressure on the water adsorption to the immobilized lipase in the SC-CO₂ was examined. Then, the continuous interesterification of triolein and stearic acid by the moist immobilized lipase was examined. The amount of water adsorption to the immobilized lipase in the supercritical carbon dioxide measured under the condition of a different temperature and pressure has been expressed by a correlation equation of Freundlich type by using relative water standardized with the solubility of water in each condition. Optimum operating conditions of the interesterification by immobilized lipase in the SC-CO₂ was 323 K, 16.9 MPa and adsorbed-water concentration of 2 wt%. The production rate obtained by enzymatic acidolysis in the SC-CO₂ was found to be about 0.03 mmol/h2g-immobilized enzyme, leaving 74% residual triglyceride at the optimum operating conditions.     

Specificity of Carica papaya latex in lipase-catalyzed interesterification reactions

Enzymatic interesterification of the chiral triacylglycerol, 1-butyroyl-2-stearoyl-3-palmitoyl-sn-glycerol (sn-BSP) with trimyristin indicated that the lipase present in Carica papaya latex exhibits an sn3 stereoselectivity. Other interesterification experiments with homogeneous triacylglycerols of varying chain length with tricaprylin showed that this enzyme also has a typoselectivity for short chain fatty acids.This revised version was published online in October 2005 with corrections to the Cover Date.     

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.     

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.     

生物印迹:一个直接的酶修饰技术

生物印迹技术是一个简单、直接的酶修饰技术,已应用到有机合成、生物传感器制备和生物分离等领域,在推动化学品绿色合成方面具有潜在的应用价值。本文在生物印迹概念的提出与发展、分类、应用以及印迹技术策略的发展等方面综述近期研究成果,针对生物印迹研究过程的现实问题,展望其未来的发展趋势,为生物印迹相关研究提供有益的借鉴。     

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