Alcoholysis catalyzed by Candida antarctica lipase B in a gas/solid system: effects of water on kinetic parameters

The influence of water on the kinetics of alcoholysis of methyl propionate and n-propanol catalyzed by immobilized lipase B from Candida antarctica was studied in a continuous solid/gas reactor. In this reactor, the solid phase is composed of a packed enzymatic sample which is percolated by gaseous nitrogen, simultaneously carrying gaseous substrates to the enzyme while removing reaction products. In this system, interactions between the enzyme and nonreacting molecules are avoided, since no solvent is present, and it is thus more easy to assess the role of water. To this end, alcohol inhibition constant, substrates dissociation constants as well as acylation rate constant and ratio of acylation to deacylation rate constants have been determined as a function of water activity (a(w)). Data obtained highlight that n-propanol inhibition constant and dissociation constant of methyl propionate are a lot affected by a(w) variations whereas water has no significant effect on the catalytic acylation step nor on the ratio of acylation to deacylation rate constants. These results suggest the water-independent character of the transition step.     

Immobilization conditions of ketoreductase on enantioselective reduction in a gas-solid bioreactor

The immobilization conditions of commercial ketoreductase for continuous enantioselective reduction in the gas-phase reaction were investigated with respect to the immobilization efficiency (residual activity and protein loading) and the gas-phase reaction efficiency (initial reaction rate, half-life, and enantioselectivity). For the analyses, ketoreductase was first immobilized by physical deposition on glass supports and the reduction of 2-butanone to (S)-2-butanol with the concomitant regeneration of NADH by 2-propanol was used as a model reaction. The optimal conditions of enzyme immobilization were obtained using an absolute pressure of 100 hPa for drying, a pH between 6.5 and 7.0, and a buffer concentration of 50 mM. The buffer concentration in particular had a strong effect on both the enzyme activity and enantioselectivity. Under optimal immobilization conditions, the thermostability of ketoreductase in the gas-phase system was enhanced compared to the aqueous-phase system, while the enantioselectivity was successfully maintained at a level identical to that of the native enzyme. These results indicate that the gas-phase reaction has a great potential for industrial production of chiral compounds, but requires careful optimization of immobilization conditions for the reaction to progress effectively.     

Kinetic studies of fusarium solani pisi cutinase used in a gas/solid system: transesterification and hydrolysis reactions

Fusarium solani cutinase supported onto Chromosorb P was used to catalyze transesterification (alcoholysis) and hydrolysis on short volatile alcohols and esters in a continuous gas/solid bioreactor. In this system, a solid phase composed of a packed enzymatic preparation was continuously percolated with carrier gas which fed substrates and removed reaction products simultaneously. A kinetic study was performed under differential operating conditions in order to get initial reaction rates. The effect of the hydration state of the biocatalyst on the kinetics was studied for 3 conditions of hydration (a(w) = 0.2, a(w) = 0.4 and a(w) = 0.6), the alcoholysis of propionic acid methyl ester with n-propanol, and for 5 hydration levels (from a(w) = 0.2 to a(w) = 0.6) for the hydrolysis of propionic acid methyl, ethyl or propyl esters. F. solani cutinase was found to have an unusual kinetic behavior. A sigmoid relationship between the rate of transesterification and the activity of methyl propionate was observed, suggesting some form of cooperative activation of the enzyme by one of its substrate. For the hydrolysis of short volatile propionic acid alkyl esters, threshold effects on the reaction rate, highly depending on the water activity and the substrate polarity, are reported. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 1-8, 1997.     

Alcoholysis catalyzed by Candida antarctica lipase B in a gas/solid system obeys a Ping Pong Bi Bi mechanism with competitive inhibition by the alcohol substrate and water.

The kinetics of alcoholysis of methyl propionate and n-propanol catalyzed by Candida antarctica lipase B supported onto silanized Chromosorb P was studied in a continuous solid/gas reactor. In this system the solid phase is composed of a packed enzymatic sample and is percolated by nitrogen as carrier gas, which simultaneously carries substrates to the enzyme while removing reaction products. In this reactor the thermodynamic activity of substrates and effectors can be perfectly adjusted allowing kinetic studies to be performed under different operating conditions. The kinetics obtained for alcoholysis were suggested to fit a Ping Pong Bi Bi mechanism with dead-end inhibition by the alcohol. The values of all apparent kinetic parameters were calculated and the apparent dissociation constant of enzyme for gaseous ester was found very low compared with the one obtained for liquid ester in organic medium, certainly due to the more efficient diffusion in the gaseous phase. The effect of water thermodynamic activity was also investigated. Water was found to act as a competitive inhibitor, with a higher inhibition constant than n-propanol. Thus alcoholysis of gaseous methyl propionate and n-propanol catalyzed by C. antarctica lipase B was found to obey the same kinetic mechanism as in other non-conventional media such as organic liquid media and supercritical carbon dioxide, but with much higher affinity for the substrates.     

Enzymatic Synthesis of Hexyl Glycosides from Lactose At Low Water Activity and High Temperature Using Hyperthermostable β-glycosidases

Optimization of hexyl-g-glycoside synthesis from lactose in hexanol at low water activity and high temperature was investigated using g-glycosidases from hyperthermophilic organisms: Sulfolobus solfataricus (LacS) and Pyrococcus furiosus (CelB). The method for water activity adjustment by equilibration with saturated salt solutions was adapted for use at high temperature. The influence of enzyme immobilization (on XAD-4, XAD-16, or Celite), addition of surfactants (AOT or SDS), substrate concentration, water activity, and temperature (60-90°C) on enzymatic activity and hexyl-g-glycoside yield were examined. Compared to other g-glycosidases in lactose conversion into alkyl glycoside, these enzymes showed high activity in a hexanol one-phase system and synthesized high yields of both hexyl-g-galactoside and hexyl-g-glucoside. Using 32 λg/l lactose (93 λmM), LacS synthesized yields of 41% galactoside (38.1 λmM) and 29% glucoside (27.0 λmM), and CelB synthesized yields of 63% galactoside (58.6 λmM) and 28% glucoside (26.1 λmM). With the addition of SDS to the reaction it was possible to increase the initial reaction rate of LacS and hexyl-g-galactoside yield (from 41 to 51%). The activity of the lyophilized enzyme was more influenced by the water content in the reaction than the enzyme on solid support. In addition, it was concluded that for the lyophilized enzyme preparation the enzymatic activity was much more influenced by the temperature when the water activity was increased. A variety of different glycosides were prepared using different alcohols as acceptors.     

Preparation and characterization of enzymes immobilized by graft copolymerization to different polysaccharides

A method of enzyme immobilization by graft copolymerization on polysaccharides is reported. Glycidylmethacrylate was used as a vinylating reagent and the reaction product with enzymes (HRP, GOD, Am, ChT) was copolymerized with different matrices (cellulose, Sepharose, Sephadex, Starch). Various factors affect the final activity of copolymers; these include the redox system, the type of support, and the quantity and type of vinyl monomer added. Using a fixed quantity of enzyme and support (3 mg enzyme, 100 mg support), the coupling efficiency varied from 2 to 50%. The most important characteristics in these immobilized systems were tested (stability in continuous washing, kinetic characteristics, storage, thermal, and lyophilization stability). Immobilized-enzyme graft copolymers have very similar kinetic behavior to that of the free enzyme. Diffusion is not seriously limited, as shown by kinetic parameters and energy activation values, and this indicates that the immobilization reaction does not alter the enzymatic activity.     

Substrate and water adsorption phenomena in a gas/solid enzymatic reactor

The adsorption of water and substrates to dry deposited alcohol dehydrogenase from Lactobacillus brevis (LBADH) is studied in a continuous enzymatic gas/solid reactor. This work is aiming at obtaining a deeper and more thorough understanding of the enzyme microenvironment in the gas/solid system of acetophenone reduction with concomitant oxidation of 2-propanol. Extensive water adsorption studies showed that the effect of sucrose in the enzyme preparation on the water adsorption isotherm is significant for water activities exceeding 0.5 and reaches a factor 2 with respect to bead mass at water activity of 0.9. Significant hysteresis during water desorption is identified, resulting in up to 0.6 mg_water/mg_protein, for lyophilized enzyme preparation and up to 10 mg_water/mg_protein for deposited enzyme preparation. The adsorption of the substrates is quantified here for the first time. Whereas the adsorption of the main substrate, acetophenone, may reach a significant level of up to 6 mg/mg_protein, at an acetophenone activity of 0.32, the secondary substrate, 2-propanol is not adsorbed at a detectable degree. The presence of water leads to a decrease of the adsorbed amount of acetophenone, by approximately 25%, at a water activity of 0.54.     

Lipase hydration state in the gas phase: sorption isotherm measurements and inverse gas chromatography

The adsorption of water and substrate on immobilized Candida antarctica lipase B was studied by performing adsorption isotherm measurements and using inverse gas chromatography (IGC). Water adsorption isotherm of the immobilized enzyme showed singular profile absorption incompatible with the Brunauer-Emmet-Teller model, probably due to the hydrophobic nature of the support, leading to very low interactions with water. IGC allowed determining the evolution with water thermodynamic activity (a(W)) of both dispersive surface energies and acidity and basicity constants of immobilized enzyme. These results showed that water molecules progressively covered immobilized enzyme, when increasing a(W), leading to a saturation of polar groups above a(W) 0.1 and full coverage of the surface above a(W) 0.25. IGC also enabled relevant experiments to investigate the behavior of substrates under a(W) that they will experience, in a competitive situation with water. Results indicated that substrates had to displace water molecules in order to adsorb on the enzyme from a(W) values ranging from 0.1 to 0.2, depending on the substrate. As the conditions used for these adsorption studies resemble the ones of the continuous enzymatic solid/gas reactor, in which activity and selectivity of the lipase were extensively studied, it was possible to link adsorption results with particular effects of water on enzyme properties.     

A broad pH range indicator-based spectrophotometric assay for true lipases using tributyrin and tricaprylin

A continuous assay is proposed for the screening of acidic, neutral, or alkaline lipases using microtiter plates, emulsified short- and medium-chain TGs, and a pH indicator. The lipase activity measurement is based on the decrease of the pH indicator optical density due to protonation which is caused by the release of FFAs during the hydrolysis of TGs and thus acidification. Purified lipases with distinct pH optima and an esterase were used to validate the method. The rate of lipolysis was found to be linear with time and proportional to the amount of enzyme added in each case. Specific activities measured with this microplate assay method were lower than those obtained by the pH-stat technique. Nevertheless, the pH-dependent profiles of enzymatic activity were similar with both assays. In addition, the substrate preference of each enzyme tested was not modified and this allowed discriminating lipase and esterase activities using tributyrin (low water solubility) and tricaprylin (not water soluble) as substrates. This continuous lipase assay is compatible with a high sample throughput and can be applied for the screening of lipases and lipase inhibitors from biological samples.     

Effect of yeast cell disruption on ADH activity for redox reactions with in situ cofactor regeneration in a continuous solid/gas bioreactor

It has recently been demonstrated that dried cells of Saccharomyces cerevisiae were able to produce alcohols and aldehydes in a solid/gas reactor with in situ cofactor regeneration. Since diffusion of gaseous substrates may be limited by the membrane and cell wall, cell disruption by sonication was used to improve oxidoreduction with ethanol and butyraldehyde as substrates. Results showed that partial cell disruption enhances the maximum conversion yield with the best results obtained after 2 min of sonication. Beyond this time, the ADH activity decreased. Better stability was observed in the pellet obtained after centrifugation indicating the importance of cell environment for enzyme stability. Tests on purified mitochondria showed that the ADH activity in cells was mainly cytoplasmic. The addition of oxidized cofactor did not change either the activity or the stability of the catalyst in a gaseous medium. The effect of water activity was studied on material obtained after 2 min of disruption and a reduction of critical water activity needed for revealing enzymatic activity was observed. With increasing a_w, the enzyme was active at a_w=0.3 while a water activity of 0.4 was required before disruption. Nevertheless, the best compromise between activity and stability was obtained in both cases for a water activity of 0.57.     

Immobilization of enzymes with polyaziridines.

A novel method of enzyme immobilization using a low molecular weight prepolymer of tri-functional aziridines which can immobilize enzymes both by covalent attachment and entrapment within a gel matrix is described. The enzymes are immobilized on a solid support and exhibit an excellent retention of enzymatic activity. The immobilization procedure is essentially a single step process which can be easily performed at room temperature or 4 degrees C in either aqueous solution or in an inert organic solvent. The polyaziridines used in the immobilization are nontoxic, available in bulk at low cost and completely miscible with water and many organic solvents, thus providing one of the most satisfactory methods of immobilization available.     

Repeated batch and continuous operations for phosphatidylglycerol synthesis from phosphatidylcholine with immobilized phospholipase D

Summary The repeated batch and continuous operations for transphosphatidylation reaction were carried out for phosphatidylglycerol (PG) synthesis from phosphatidylcholine (PC) with the help of immobilized cabbage phospholipase D (PLD) in the presence of glycerol. The biphasic reaction system was used which included the aqueous phase containing immobilized PLD along with high concentrations of glycerol (30%–50%) and buffer, whereas the main part of substrate (PC) and products (mainly PG) formed were in the organic phase (diethyl ether).Octyl-Sepharose CL-4B having a hydrophobic octyl group was chosen for the PLD immobilization. Both immobilization yield and activity yield of immobilized enzyme were 100%. The effects of solvents, temperature and glycerol concentrations on the immobilized PLD were examined. Repeated batch conversion of PC (15 g/l) to PG was examined with the immobilized PLD in 30% glycerol. In all five batch cycles examined, 100% selectivity was obtained and there was no significant decrease in the fractional conversion of PC to PG (98%–99%) in the first three batch cycles. In the cases of a packed-bed reactor (PBR) and a continuous stirred-tank reactor (CSTR) used for continuous synthesis of PG with the immobilized PLD, the operational stabilities of the immobilized enzyme were almost the same (half life=14 h at 30°C) when purified PC was used, while in the case of partially purified PC in CSTR the half life increased more than five times.Abbreviations used PC phosphatidylcholine - PG phosphatidylglycerol - PA phosphatidic acid - PLD phospholipase D - PBR packed bed reactor - CSTR continuous stirred tank reactor Studies on enzymatic conversion of phospholipids (III)     

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.     

Enzymatic Synthesis of Hexyl Glycosides from Lactose At Low Water Activity and High Temperature Using Hyperthermostable β-glycosidases

Optimization of hexyl-&#103-glycoside synthesis from lactose in hexanol at low water activity and high temperature was investigated using &#103-glycosidases from hyperthermophilic organisms: Sulfolobus solfataricus (LacS) and Pyrococcus furiosus (CelB). The method for water activity adjustment by equilibration with saturated salt solutions was adapted for use at high temperature. The influence of enzyme immobilization (on XAD-4, XAD-16, or Celite), addition of surfactants (AOT or SDS), substrate concentration, water activity, and temperature (60-90°C) on enzymatic activity and hexyl-&#103-glycoside yield were examined. Compared to other &#103-glycosidases in lactose conversion into alkyl glycoside, these enzymes showed high activity in a hexanol one-phase system and synthesized high yields of both hexyl-&#103-galactoside and hexyl-&#103-glucoside. Using 32 &#117 g/l lactose (93 &#117 mM), LacS synthesized yields of 41% galactoside (38.1 &#117 mM) and 29% glucoside (27.0 &#117 mM), and CelB synthesized yields of 63% galactoside (58.6 &#117 mM) and 28% glucoside (26.1 &#117 mM). With the addition of SDS to the reaction it was possible to increase the initial reaction rate of LacS and hexyl-&#103-galactoside yield (from 41 to 51%). The activity of the lyophilized enzyme was more influenced by the water content in the reaction than the enzyme on solid support. In addition, it was concluded that for the lyophilized enzyme preparation the enzymatic activity was much more influenced by the temperature when the water activity was increased. A variety of different glycosides were prepared using different alcohols as acceptors.     

Immobilized Candida antarctica lipase B: Hydration, stripping off and application in ring opening polyester synthesis

This work reviews the stripping off, role of water molecules in activity, and flexibility of immobilized Candida antarctica lipase B (CALB). Employment of CALB in ring opening polyester synthesis emphasizing on a polylactide is discussed in detail. Execution of enzymes in place of inorganic catalysts is the most green alternative for sustainable and environment friendly synthesis of products on an industrial scale. Robust immobilization and consequently performance of enzyme is the essential objective of enzyme application in industry. Water bound to the surface of an enzyme (contact class of water molecules) is inevitable for enzyme performance; it controls enzyme dynamics via flexibility changes and has intensive influence on enzyme activity. The value of pH during immobilization of CALB plays a critical role in fixing the active conformation of an enzyme. Comprehensive selection of support and protocol can develop a robust immobilized enzyme thus enhancing its performance. Organic solvents with a log P value higher than four are more suitable for enzymatic catalysis as these solvents tend to strip away very little of the enzyme surface bound water molecules. Alternatively ionic liquid can work as a more promising reaction media. Covalent immobilization is an exclusively reliable technique to circumvent the leaching of enzymes and to enhance stability. Activated polystyrene nanoparticles can prove to be a practical and economical support for chemical immobilization of CALB. In order to reduce the E-factor for the synthesis of biodegradable polymers; enzymatic ring opening polyester synthesis (eROPS) of cyclic monomers is a more sensible route for polyester synthesis. Synergies obtained from ionic liquids and immobilized enzyme can be much effective eROPS.     

Effect of yeast cell disruption on ADH activity for redox reactions with in situ cofactor regeneration in a continuous solid/gas bioreactor

It has recently been demonstrated that dried cells of Saccharomyces cerevisiae were able to produce alcohols and aldehydes in a solid/gas reactor with in situ cofactor regeneration. Since diffusion of gaseous substrates may be limited by the membrane and cell wall, cell disruption by sonication was used to improve oxidoreduction with ethanol and butyraldehyde as substrates. Results showed that partial cell disruption enhances the maximum conversion yield with the best results obtained after 2 min of sonication. Beyond this time, the ADH activity decreased. Better stability was observed in the pellet obtained after centrifugation indicating the importance of cell environment for enzyme stability. Tests on purified mitochondria showed that the ADH activity in cells was mainly cytoplasmic. The addition of oxidized cofactor did not change either the activity or the stability of the catalyst in a gaseous medium. The effect of water activity was studied on material obtained after 2 min of disruption and a reduction of critical water activity needed for revealing enzymatic activity was observed. With increasing a_w, the enzyme was active at a_w=0.3 while a water activity of 0.4 was required before disruption. Nevertheless, the best compromise between activity and stability was obtained in both cases for a water activity of 0.57.     

Gluco-oligosaccharide synthesis by free and immobilized beta-glucosidase

Gluco-oligosaccharides were synthesized through the enzymatic condensation of D-glucose at high concentration using a commercial almond beta-glucosidase. The synthesis reactions were carried out with both free and immobilized enzyme, with or without sorbitol, an efficient depressor of water activity (a(w)) in the presence of different glucose concentrations. The yield and the composition of the gluco-oligosaccharides produced changed with the reaction mixture and the form of the enzyme used (free or immobilized). The use of 5 M glucose solution permitted only disaccharides to be obtained, whereas with a glucose concentration of 7.5 M glucose, di-, tri-, and tetrasaccharides were produced. A 7.5 M glucose solution used with 4.4 M sorbitol gave three times more disaccharides than the same solution without sorbitol. Moreover, the immobilized enzyme was much more active in synthesis. The synthesis yield (oligomers mg/mL . mg of enzyme) after immobilization was 573% compared to that of the free enzyme, when a 7.5 M glucose solution was tested. The effects of substrate concentration, sorbitol addition and enzyme immobilization were investigated. (c) 1993 John Wiley & Sons, Inc.     

γ-Fe_2O_3-凹土超顺磁性纳米复合材料固载猪胰脂肪酶

以凹凸棒石黏土为原料,制备γ-Fe2O3-凹土超顺磁性纳米复合材料(γ-Fe2O3-ATP)作为猪胰脂肪酶(PPL)固定化的载体,利用透射电子显微镜(TEM)、N2吸附脱附等温图(BET)、振动试样磁强计(VSM)等对材料进行表征,同时对固定化条件和固定化酶的相关性质进行了研究。结果表明:制备的γ-Fe2O3-ATP是介孔材料,比表面积为102.63 m2/g,平均孔径为10.862 nm,饱和磁化强度为8.915 emu/g,其作为载体能实现固定化酶与反应介质简单、快速分离回收和重复利用。在固定化时间为4 h及pH 6.0时制备的固定化酶效果最佳;经过6 h高温保存后固定化酶可保留初始酶活的52%,而游离酶仅保留初始酶活的19%,同时固定化酶在重复使用5次后酶活仍保留初始酶活的60%。     

Gas phase acetaldehyde production in a continuous bioreactor

The gas phase continuous production of acetaldehyde was studied with particular emphasis on the development of biocatalyst (alcohol oxidase on solid phase support materials) for a fixed bed reactor. Based on the experimental results in a batch bioreactor, the biocatalysts were prepared by immobilization of alcohol oxidase on Amberlite IRA-400, packed into a column, and the continuous acetaldehyde production in the gas phase by alcohol oxidase was performed. The effects of the reaction temperature, flow rates of gaseous stream, and ethanol vapor concentration on the performance of the continuous bioreactor were investigated. (c) 1993 John Wiley & Sons, Inc.     

Enzymatic surface-initiated polymerization: a novel approach for the in situ solid-phase synthesis of biocompatible polymer poly(3-hydroxybutyrate)

A novel system for surface-initiated enzymatic polymerization of a film of polyhydroxyalkanoate (PHA) on solid surfaces has been developed and characterized. PHAs are aliphatic polyesters produced by a variety of microorganisms as a reserve of carbon and energy, and their properties range from elastomers to thermoplastics, depending on their monomeric composition. The PHA synthase from Ralstonia eutropha H16 was expressed as a poly-histidine fusion in Escherichia coli and immobilized onto several solid substrates through a transition-metal complex, Ni(2+)-nitrilotriacetic acid. The immobilized PHA synthase catalyzed the surface-initiated polymerization of 3-(R)-hydroxybutyryl-CoA, forming a polymer film with a uniform thickness on the surface. In this work, we describe the patterned immobilization of the intact enzyme on silicon and subsequent enzymatic polymerization. The immobilized enzyme had a lower specific activity and did not exhibit a lag phase as compared to the soluble enzyme.