Lipase catalyzed esterification of glycidol in nonaqueous solvents: solvent effects on enzymatic activity

We studied the effect of organic solvents on the kinetics of porcine pancreatic lipase (pp) for the resolution of racemic glycidol through esterification with butyric acid. We quantified ppl hydration by measuring water sorption isotherms for the enzyme in the solvents/mixtures tested. The determination of initial rates as a function of enzyme hydration revealed that the enzyme exhibits maximum apparent activity in the solvents/mixtures at the same water content (9% to 11% w/w) within the associated experimental error. The maximum initial rates are different in all the media and correlate well with the logarithm of the molar solubility of water in the media, higher initial rates being observed in the solvents/mixtures with lower water solubilities. The data for the mixtures indicate that ppl apparent activity responds to bulk property of the solvent. Measurements of enzyme particle sizes in five of the solvents, as function of enzyme hydration, revealed that mean particle sizes increased with enzyme hydration in all the solvents, differences between solvents being more pronounced at enzyme hydration levels close to 10%. At this hydration level, solvents having a higher water content lead to lower reaction rates; these are the solvents where the mean enzyme particle sizes are greater. Calculation of the observable modulus indicates there are no internal diffusion limitations. The observed correlation between changes in initial rates and changes in external surface area of the enzyme particles suggests that interfacial activation of ppl is only effective at the external surface of the particles. Data obtained for the mixtures indicate that ppl enantioselectivity depends on specific solvent-enzyme interactions. We make reference to ppl hydration and activity in supercritical carbon dioxide. (c) 1994 John Wiley & Sons, Inc.     

Solvent effects on the catalytic activity of subtilisin suspended in compressed gases

We studied a model transesterification reaction catalyzed by subtilisin Carlsberg suspended in carbon dioxide, propane, and mixtures of these solvents under pressure. To account for solvent effects due to differences in water partitioning between the enzyme and the bulk solvents, we measured water sorption isotherms for the enzyme in each solvent. We measured catalytic activity as a function of enzyme hydration and obtained bell-shaped curves with maxima at the same enzyme hydration (12%) in all the solvents. However, the activity maxima were different in all media, being much higher in propane than in either CO(2) or the mixtures with 50 and 10% CO(2). Considerations based on the solvation ability of the solvents did not offer an explanation for the differences in catalytic activity observed. Our results suggest that CO(2) has a direct adverse effect on the catalytic activity of subtilisin. (c) 1996 John Wiley & Sons, Inc.     

Lysozyme kinetics in low water activity media. A possible hydration memory

The influence of water activity on initial lysozyme kinetics is studied. Enzyme catalytic capacity exponentially increases with thermodynamical water activity of the reactant medium; this relation seems independent of the chemical structure of the water activity depressors but dependent on the structuration of water molecules they induce. This influence of water organization on initial enzyme activity is immediate and may be preserved even after a large dilution, thus lysozyme presents a "hydration memory" phenomenon. This effect is in accordance with sorption/desorption isotherms, an hysteresis loop being observed.     

Solvent effects on the catalytic activity of subtilisin suspended in organic solvents

We studied a model transesterification reaction catalyzed by subtilisin Carlsberg suspended in toluene, n-hexane, diisopropyl ether, and mixtures of these solvents. To account for solvent effects due to differences in water partitioning between the enzyme and the bulk solvents, we measured water sorption isotherms for the enzyme in each solvent. We measured catalytic activity as a function of enzyme hydration and obtained bell-shaped curves with maxima at the same enzyme hydration in all the solvents. However, the activity maxima were different in all the media, being the lowest in toluene. Differences in the partitioning of substrates and product between the bulk solvent phase and the enzyme active site were accounted for but could not explain the lower catalytic activity observed in toluene. The fact that toluene is very similar to one of the substrates suggested the possibility of competitive inhibition by this solvent. We derived a model allowing for differences in solvation of the substrates, by using thermodynamic activities instead of concentrations, as well as for competitive inhibition by toluene. The model fit the experimental data well, confirming that toluene had a direct adverse effect on the catalytic activity of the enzyme. (c) 1996 John Wiley & Sons, Inc.     

A comparison of lipase-catalysed ester and lactone synthesis in low-water systems: analysis of optimum water activity.

We investigated the effects of the lyophilisation medium (enzyme plus buffer salt and additives) and of water activity (a(w)) on the catalytic properties of lipase from Chromobacterium viscosum (lipase CV) in organic solvents; catalysis of ester and lactone synthesis were compared and, despite the similarities of the reactive groups involved in these reactions, some interesting differences were observed. Including 2-[N-morpholino]ethanesulfonic acid (MES) buffer in the lyophilisation medium of lipase CV increased its catalytic activity in transesterification and lactonisation, although the buffer salt requirement for maximal activity differed between the two reactions. Sorbitol, glucose, lactose, 18-crown-6 (crown ether 18-C-6), beta-cyclodextrin and bovine serum albumin were employed as alternative additives in the transesterification reaction, but were not as effective as MES buffer. Salt hydrates were used to investigate the effect of a(w) on esterification and lactonisation reactions catalysed by lipase CV. The maximum rate of hexadecanolide synthesis in toluene occurred at a(w) = 0.48. The optimum a(w) for the transesterification reaction in heptane/alcohol mixtures depended on the alcohol substrate employed (1-heptanol, 2-heptanol, or 3-methyl-3-hexanol) but not on the acyl donor (p-NP acetate or caprylate). The optimum a(w) values for both reactions were unchanged when a common solvent system (toluene/1-heptanol) was employed, indicating that the dependence of enzyme activity on a(w) is an intrinsic property of the enzyme-catalysed reaction and not a function of the solvent or other additives.     

展示南极假丝酵母脂肪酶B的毕赤酵母全细胞催化合成短链芳香酯

展示酶的酵母细胞作为全细胞催化剂,既具有固定化酶的优点,又有制备简单、成本较低的特点。本研究将细胞表面展示南极假丝酵母脂肪酶B(Candida antarctica lipase B,CALB)的重组毕赤酵母用于非水相中催化合成短链芳香酯,通过滴定和气相色谱的方法测定底物酸的转化率,从底物的碳链长度、醇的结构、酵母冻干粉的添加量、底物浓度及底物的酸醇摩尔比等方面考察了展示CALB的毕赤酵母全细胞催化合成短链芳香酯的特性。研究结果表明:该全细胞催化剂可催化C10以下的酸和醇直接酯化合成多种短链芳香酯,酸的转化率达到90%以上;其中己酸和乙醇为酶的最适底物;酵母冻干粉的添加量20g/L(306.0U/g-drycell)、己酸浓度0.8mol/L、酸醇摩尔比1:1.1是合成己酸乙酯的最佳条件。在此条件下反应1.5h,己酸的转化率达到97.3%。在现有的关于脂肪酶非水相催化合成短链芳香酯的报道中,该全细胞催化剂显示出较好的底物耐受性以及较高的催化反应速率。因此,展示CALB的毕赤酵母全细胞催化剂在合成短链芳香酯方面具有较大的商业化应用潜能。     

An integrated process: ester synthesis in an enzymatic membrane reactor and water sorption

In the case of such reactions as ester synthesis, water is produced during the reaction. Because these reactions are carried out in hydrophobic solvents an additional (water) phase in the system must not be allowed, i.e. the concentration of water saturation in the organic solvent should not be exceeded. In such a case, the reaction kinetics and product equilibrium concentration undergo undesirable changes because of the partition coefficient of the components and hampered process of product separation. Hence, removal of the water produced in the reaction determines whether the process is successful or not. For this purpose, the integrated process with water sorption in the column with molecular sieves was applied. Integration of the process of synthesis and dehydration of a reaction phase, in which a biocatalyst is suspended and not dissolved as in water solutions, requires holding up of the catalyst in the reactor before directing the stream of reaction mixture to dehydration process. This hold-up and a possibility of multiple use of the catalyst may be accomplished by using a separating barrier, e.g. an ultrafiltration membrane or by permanent fixing of the catalyst to the matrix, e.g. a polymeric membrane. The efficiency and activity of a biocatalyst (lipase CAL-B) immobilized on a polymer membrane by sorption and chemical binding, were determined. A subject of study was the synthesis of geranyl acetate, one of the most known aromatic compound. A hydrophobic (polypropylene) matrix was shown to be a much better carrier in the reactions performed in an organic solvent than a hydrophilic (polyamide) membrane being tested. The reaction kinetics of geranyl acetate synthesis with the use of geraniol and acetic acid as substrates, was described by the equation defining the "Ping-Pong Bi Bi" mechanism that was related additionally to the inhibition of a substrate (acetic acid). The following constants of kinetic equation were obtained k(3)(')=0.344 mol g(-1)h(-1), K(mA)=0.257 mol l(-1), K(mG)=1.629 and K(iA)=0.288 for the native enzyme and v(max,Gel)=111.579 mol l(-1)h(-1), K(mA)=0.255 mol l(-1), K(mG)=1.91 mol l(-1), K(iA)=0.238 mol l(-1) for the one immobilized by sorption on a polypropylene membrane. Half-life time of the native enzyme activity was 204 h and stability of the immobilized preparation was 70 h. With respect to the reaction kinetics and stability of the native enzyme and immobilized preparation, from both types of membrane bioreactor more attractive appears to be the one in which the membrane is used not as a catalyst layer but only as a barrier that immobilizes the native enzyme within the bioreactor volume. When an integrated process proceeds, the method to collect water in the sorption column during the process, appeared to work very well. The reaction proceeded with a very high efficiency (after 120 h alpha=98.2% for native enzyme and 83.2% for immobilized enzyme) and due to low water concentration in the system ( approximately 0.000% v/v) the second phase was not created.     

Extraordinary enantiospecificity of lipase catalysis in organic media induced by purification and catalyst engineering

A purified lipase preparation from Candida rugosa was compared to its crude counterpart in anhydrous and slightly hydrated hydrophobic organic solvents. The purified lipase preparation was less active than the crude enzyme in dry n-heptane, whereas the presence of small concentrations of added water dramatically activated the purified enzyme but not the crude enzyme. Thus, in the presence of as little as 0.25 muL/mL of added water in n-heptane, the purified enzyme is over 230-fold more active and 6-fold more enantioselective than the dry enzyme suspension in the esterification of racemic 2-(4-chlorophenoxy)propionic acid with n-butanol. The reactivity and selectivity of this biocatalyst, however, was affected by coalescence of the enzyme preparation suspended in the wet organic solvent. Engineering the biocatalyst environment by dissolving the purified lipase in aqueous buffer and then adding this solution to n-heptane resulted in a precipitated enzyme preparation with smaller particle sizes that did not coalesce severely. In the presence of 5 muL/mL of water added with the enzyme, this pretreatment resulted in an activation over the dry, purified enzyme preparation of over 1800-fold and nearly enantiospecific catalysis (E > 100). Hence, by simply modifying the way enzymes are hydrated, dramatic activation of catalytic competency can be achieved. (c) 1996 John Wiley & Sons, Inc.     

The biocatalytic activity of bromelain in ester synthesis reaction: difference between the intrinsic lipase activity and thermal catalysis

Biocatalytic activities of bromelain preparations were carried out in proteolytic (4500 units g^–1), lipolytic (67 units g^–1) and, more particularly, in fatty acid ester synthetic reactions. The ester synthesis reactions were studied and several thermodynamic parameters and non-biological reference reactions were also investigated. Only temperature had a strong influence on the maximum reaction yield (30% after 10 days) and revealed that thermal catalysis, which exists in esterification, raises doubts concerning the real biocatalytic activity of the plant extract. When this thermal catalysis is taken into account, the intrinsic lipase activity of the bromelain preparations in esterification reactions is nil.     

Modification of hydrophilicity/hydrophobicity of the microenvironment of lipase of Candida rugosa by dextrans

Replacing the lactose used in the commercial preparation of lipase from Candida rugosa by dextrans with different molecular weight, several preparations with enhanced activities in esterification of (R,S)-ibuprofen in organic medium were obtained. The presence of carbohydrates modifies the microenvironment of the enzyme and maintains the hydration of the biocatalyst. We can modulate the hydrophilic/hydrophobic balance on the surface of the biocatalyst creating non covalent enzyme-dextran complexes.     

Immobilization of lipase B from Candida antarctica on porous styrene-divinylbenzene beads improves butyl acetate synthesis

A new biocatalyst of lipase B from Candida antarctica (MCI-CALB) immobilized on styrene-divinylbenzene beads (MCI GEL CHP20P) was compared with the commercial Novozym 435 (immobilized lipase) in terms of their performances as biocatalysts for the esterification of acetic acid and n-butanol. The effects of experimental conditions on reaction rates differed for each biocatalyst, showing different optimal values for water content, temperature, and substrate molar ratio. MCI-CALB could be used at higher acid concentrations, up to 0.5 M, while Novozym 435 became inactivated at these acid concentrations. Although Novozym 435 exhibited 30% higher initial activity than MCI-CALB for the butyl acetate synthesis, the reaction course was much more linear using the new preparation, meaning that the MCI-CALB allows for higher productivities per cycle. Both preparations produced around 90% of yield conversions after only 2 h of reaction, using 10% (mass fraction) of enzyme. However, the main advantage of the new biocatalyst was the superior performance during reuse. While Novozym 435 was fully inactivated after only two batches, MCI-CALB could be reused for six consecutive cycles without any washings and keeping around 70% of its initial activity. It is proposed that this effect is due to the higher hydrophobicity of the new support, which does not retain water or acid in the enzyme environment. MCI-CALB has shown to be a very promising biocatalyst for the esterification of small-molecule acids and alcohols.     

Water Binding in Legume Seeds

The physical status of water in seeds has a pivotal role in determining the physiological reactions that can take place in the dry state. Using water sorption isotherms from cotyledon and axis tissue of five leguminous seeds, the strength of water binding and the numbers of binding sites have been estimated using van't Hoff analyses and the D'Arcy/Watt equation. These parameters of water sorption are calculated for each of the three regions of water binding and for a range of temperatures. Water sorption characteristics are reflective of the chemical composition of the biological materials as well as the temperature at which hydration takes place. Changes in the sorption characteristics with temperature and hydration level may suggest hydration-induced structural changes in cellular components.     

Adsorptive control of water in esterification with immobilized enzymes: II. fixed-bed reactor behavior

Experimental and theoretical studies are conducted to understand the dynamic behavior of a continuous-flow fixed-bed reactor in which an esterification is catalyzed by an immobilized enzyme in an organic solvent medium. The experimental system consists of a commercial immobilized lipase preparation known as Lipozyme as the biocatalyst, with propionic acid and isoamyl alcohol (dissolved in hexane) as the reaction substrates. A complex dynamic behavior is observed experimentally as a result of the simultaneous occurrence of reaction and adsorption phenomena. Both propionic acid and water are adsorbed by the biocatalyst resulting in lower reaction rates. In addition, an excessive accumulation of water in the reactor leads to a rapid irreversible inactivation of the enzyme. A model based on previously-obtained adsorption isotherms and kinetic expressions, as well as on adsorption rate measurements obtained in this work, is used to predict the concentration and thermodynamic activity of water along the reactor length. The model successfully predicts the dynamic behavior of the reactor and shows that a maximum thermodynamic activity of water occurs at a point at some distance from the reactor entrance. A cation exchange resin in sodium form, packed in the reactor as a selective water adsorbent together with the catalyst particles, is shown to be an effective means for preventing an excessive accumulation of water formed in the reaction. Its use results in longer cycle times and greater productivity. As predicted by the model, the experimental results show that the water adsorbed on the catalyst and on the ion exchange resin can be removed with isoamyl alcohol with no apparent loss in enzyme activity.     

Screening of plant peptidases for the synthesis of arginine-based surfactants

Partially purified preparations with proteolytic activity, obtained from South American native plants, were used as biocatalysts in condensation reactions of N-protected arginine alkyl ester derivatives with decylamine and dodecylamine in low-water content systems. The final products are cationic surfactants with potential application as emulsifiers and preservatives. Most of the proteolytic extracts were obtained from latex of species belonging to the Asclepiadaceae family (araujiain from Araujia hortorum, asclepain c from Asclepias curassavica and funastrain from Funastrum clausum). Hieronymain was obtained from unripe fruits of Bromelia hieronymi (Bromeliaceae). Plant proteases from commercial sources (papain and bromelain) were also tested as catalysts in the same reactions. Araujiain and funastrain furnished good reaction conversions (60–84%, with a ratio synthesis/hydrolysis of 2–5) similar to those obtained with commercial papain. Moreover, araujiain was the biocatalyst which rendered the best conversions (60%) for the synthesis of the two novel Bz-Arg-NH-dodecylamide (Bz-Arg-NHC₁₂) and Bz-Arg-NH-decylamide (Bz-Arg-NHC₁₀) derivatives. Moderate to poor conversions (10–50%, showing a ratio synthesis/hydrolysis of 0.5–1) were achieved with asclepain c, hieronymain and bromelain. The screening presented in this work revealed that, although these are structurally similar, their behavior for the synthesis of this kind of products differ among them.     

Characteristics of immobilized lipase on hydrophobic superparamagnetic microspheres to catalyze esterification

A novel immobilized lipase (from Candida rugosa) on hydrophobic and superparamagnetic microspheres was prepared and used as a biocatalyst to catalyze esterification reactions in diverse solvents and reaction systems. The results showed that the immobilized lipase had over 2-fold higher activities in higher log P value solvents. An exponential increase of lipase activity against log P of two miscible solvent mixtures was observed for the first time. Both free and immobilized lipase achieved its maximum activity at the range of water activity (a(w)) 0.5-0.8 or higher. At a(w) 0.6, the immobilized lipase exhibited markedly higher activities in heptane and a solvent-free system than did the native lipase. In multicompetitive reactions, the alcohol specificity of the lipase showed a strong chain-length dependency, and the immobilized enzyme exhibited more preference for a longer-chain alcohol, which is different from previous reports. The immobilized lipase showed higher specificities for butyric acid and the medium-chain-length fatty acids (C(8)-C(12)). Then, the immobilized lipase was extended to solvent-free synthesis of glycerides from glycerol and fatty acids. Recovered by magnetic separation, the immobilized lipase exhibited good reusability in repeated batch reaction, indicating its promising feature for biotechnology application.     

Effect of water activity on enzyme hydration and enzyme reaction rate in organic solvents

The effects of water on enzyme (protein) hydration and catalytic efficiency of enzyme molecules in organic solvents have been analyzed in terms of the thermodynamic activity of water, which has been estimated by the NRTL or UNIFAC equations. When the amount of water bound to the enzyme was plotted as a function of water activity, the water adsorption isotherms obtained from the water-solvent liquid mixtures were similar to the reported water-vapor adsorption isotherms of proteins. The water adsorption of proteins from the organic media was not significantly dependent on the properties of the solvents or the nature of the proteins. It is also shown that there is a linear relationship between the logarithm of the enzyme reaction rate and water activity. However, the dependence of the enzyme reaction rate on water activity was found to be different depending on the properties of the solvent. The relationship between water activity and other solvent parameters such as solvent hydrophobicity and the solubility of water in the solvent is also discussed.     

Magnetic Cross-Linked Enzyme Aggregates (mCLEAs) of Candida antarctica Lipase: An Efficient and Stable Biocatalyst for Biodiesel Synthesis

Enzyme-catalyzed production of biodiesel is the object of extensive research due to the global shortage of fossil fuels and increased environmental concerns. Herein we report the preparation and main characteristics of a novel biocatalyst consisting of Cross-Linked Enzyme Aggregates (CLEAs) of Candida antarctica lipase B (CALB) which are covalently bound to magnetic nanoparticles, and tackle its use for the synthesis of biodiesel from non-edible vegetable and waste frying oils. For this purpose, insolubilized CALB was covalently cross-linked to magnetic nanoparticles of magnetite which the surface was functionalized with –NH₂ groups. The resulting biocatalyst combines the relevant catalytic properties of CLEAs (as great stability and feasibility for their reutilization) and the magnetic character, and thus the final product (mCLEAs) are superparamagnetic particles of a robust catalyst which is more stable than the free enzyme, easily recoverable from the reaction medium and reusable for new catalytic cycles. We have studied the main properties of this biocatalyst and we have assessed its utility to catalyze transesterification reactions to obtain biodiesel from non-edible vegetable oils including unrefined soybean, jatropha and cameline, as well as waste frying oil. Using 1% mCLEAs (w/w of oil) conversions near 80% were routinely obtained at 30°C after 24 h of reaction, this value rising to 92% after 72 h. Moreover, the magnetic biocatalyst can be easily recovered from the reaction mixture and reused for at least ten consecutive cycles of 24 h without apparent loss of activity. The obtained results suggest that mCLEAs prepared from CALB can become a powerful biocatalyst for application at industrial scale with better performance than those currently available.     

Optimization of methyl propionate production catalysed by Mucor miehei lipase

Lipase from Mucor miehei was used to catalyse the esterification reaction between propionic acid and methyl alcohol in modified organic media. Small-scale model studies were performed in order to define the optimal conditions. The specific activity of immobilized lipase, adsorbed onto hydrophilic supports, compared to free lipase, showed that enzyme activity was altered by immobilisation. Non-polar solvents were shown to be less harmful for the biocatalyst than solvents with higher polarity. Diethyl ether was used as the cosolvent of hexane to improve the solubility of substrates in the organic phase thus increasing contact with enzyme. An optimal ratio of 90/10 (v/v) was determined for a hexane/diethyl ether mixture. The mass of enzyme preparation must be high enough to display optimal diffusion of the reagents and hydration of the catalytic sites. Increased substrate concentrations were stimulatory up to a point after which inhibition and enzyme destabilisation, in repeated runs, occurred. Water saturation of the organic medium greatly lowered the biosynthetic activity of the enzyme. It was possible to reach a 96% methyl propionate biosynthesis yield after 2.30 h reaction, underlining the free-enzyme operational capacity in a quasi-anhydrous modified organic medium.     

Esterification reactions of lipase in reverse micelles

The activities of lipase from Candida cylindracea and Rhizopus delemar have been investigated in water/AOT/iso-octane reverse micellar media through the use of two esterification reactions: fatty acid-alcohol esterification and glyceride synthesis. Such media promotes the occurrence of these two lipase-catalyzed reactions due to its low water content. The effect of various parameters on the activity of lipase from C. cylindracea in reverse micelles was determined and compared to results where alternate media were employed. It was observed that the structure of the media, as dictated by the type and concentration of the substrates and products and by the water/AOT ratio, w(0), had a strong impact on enzyme activity. Strong deactivation of both typase types occurred in reverse micelles, especially in the absence of substrates and for w(0) values greater than 3.0. Glyceride synthesis was realized with lipase from R. delemar, but not with that from C. cylindracea; the temperature and concentration of substrates and water strongly dictated the reaction rate and the percent conversion.     

The control of lipase-catalysed transesterification and esterification reaction rates. Effects of substrate polarity, water activity and water molecules on enzyme activity

The reaction rate of two lipase-catalysed reactions, esterification and transesterification, were studied in a liquid/solid two-phase system in order to investigate the effect of water partition between the enzyme preparation and the liquid phase composed of only the reactants, i.e. without the conventional solvents. Lipase from Candida cylindracea was used for these studies. The enzyme was inactive in dehydrated systems. In the case of monoester synthesis, the reaction rate increased with increasing water activity. The reaction rates of the non-specific C. cylindracea lipase-catalysed reactions were very sensitive to the nature of the substrates in this unusual system. For instance, the transesterification reaction rate of ethyl propionate was 48 times higher with nonanol than heptanol in the case of dehydrated substrates, but only 2.2 times higher in the case of water-saturated substrates. The results presented here demonstrate the absolute necessity to consider the polarity of every substrate, because of its ability to modify the water partition between the solid phase (enzyme preparation) and the liquid phase (substrate and product), which results in drastic changes in enzyme activity. Contrary to esterification, which is known to be activated by the water produced, the rate of transesterification remained constant at the beginning of the reaction. However, when transesterification and esterification were carried out in the same liquid phase, the transesterification reaction rate was controlled by the water produced by the concomitant esterification. Activation effects of the water molecules produced during the enzymatic reaction were of exactly the same order of magnitude for both reactions.