Continuous hydrolysis of oil by immobilized lipase in a countercurrent reactor

Lipase from Pseudomonas fluorescens biotype I was immobilized by adsorption of anion exchange resin using glutaraldehyde to enhance the adsorption. The activity yield of the immobilized lipase was very low (below 1%) when lipase activity was measured using emulsion substrate. The activity yield was 10-70% when lipase activity was measured using non-emulsion substrate. Countercurrent reactors for hydrolysis of oil using non-emulsion substrate were studied. A fluidized bed reactor was found to be superior to a fixed bed one since in a fixed bed reactor the separation rate of the two layers was slow and the flow rate of the reactor had to be slower than the separation rate. A fluidized bed reactor system equipped with settling compartments and stirring compartments was devised. Continuous lipolysis at 60 degrees C and continuous separation of oily product and water soluble product were performed. After continuous operation for more than 3 months, 70% of the initial activity of the immobilized lipase was observed at the end of the reaction.     

An approximate analytical solution to the lag period of monophenolase activity of tyrosinase

Tyrosinase shows a lag period in its action on monophenols (l-tyrosine). We propose an approximate analytical solution for the lag period, which fulfils the dependences with regard to initial enzyme concentration, and initial monophenol concentration. Furthermore, from a study of the dependences of the lag period on these variables, we can determine experimentally the o-diphenol concentration in the steady state. The Michaelis constant of the o-diphenol in the presence of the monophenol can be determined from the relationship between the o-diphenol concentration in the steady state and the initial monophenol concentration, taking into consideration the experimentally calculated Michaelis constant for the monophenol substrate. Although this Michaelis constant is much lower than the Michaelis constant for diphenol in the absence of monophenol, the binding site is the same. A kinetic analysis of the action mechanism of tyrosinase explains this difference in the values of the Michaelis constants.     

Continuous immobilized cell reactor for amide hydrolysis

Summary This article deals with continuous hydrolysis of acrylamide into acrylic acid using the wild-typeBrevibacterium sp. R312 which can hydrolyze all water-soluble amides into their corresponding acids. Biotransformation has been carried out in a fluidized bed reactor specially designed to obtain good contact conditions between cells entrapped into small calcium alginate beads (2–3 mm) and low-concentration acrylamide solutions (10–40g·l^–1). Different flow rates, biocatalyst loads and substrate concentrations have been investigated. Kinetic constants for the immobilized enzyme have been identified. It appears that the Michaelis constant does not change with operating conditions and remains roughly equal to the value obtained for free cells. In contrast, the maximum rate of hydrolysis is considerably decreased, as if only cells on the outskirts of beads were involved in the transformation. On the whole it is proved that corynebacteria cells could be usefully used for the bioconversion of amides in a continuous immobilized cell reactor; the higher the solid hold-up and/or the smaller the beads, the more efficient the biological transformation.     

Ceramic membrane microfilter as an immobilized enzyme reactor.

This study investigated the use of a ceramic microfilter as an immobilized enzyme reactor. In this type of reactor, the substrate solution permeates the ceramic membrane and reacts with an enzyme that has been immobilized within its porous interior. The objective of this study was to examine the effect of permeation rate on the observed kinetic parameters for the immobilized enzyme in order to assess possible mass transfer influences or shear effects. Kinetic parameters were found to be independent of flow rate for immobilized penicillinase and lactate dehydrogenase. Therefore, neither mass transfer nor shear effects were observed for enzymes immobilized within the ceramic membrane. Both the residence time and the conversion in the microfilter reactor could be controlled simply by regulating the transmembrane pressure drop. This study suggests that a ceramic microfilter reactor can be a desirable alternative to a packed bed of porous particles, especially when an immobilized enzyme has high activity and a low Michaelis constant.     

Catalytic properties and active-site structural features of immobilized horse liver alcohol dehydrogenase

Alcohol dehydrogenase from horse liver was immobilized by covalent attachment to CNBr-Sepharose and by adsorption to octyl-Sepharose CL-4B, a hydrophobic analog of Sepharose. In each case, rate constants for the binding and release of coenzyme and for the oxidation of substrates were measured based on the concentration of accessible active-site zinc atoms determined by titration with a paramagnetic inhibitor. All rate constants were substantially reduced upon immobilization; however, the rate constant of immobilized enzyme for ethanol oxidation was independent of the immobilization method, whereas the rate constant for cyclohexanol oxidation was lower for enzyme immobilized to octyl-Sepharose. Consequently, the substrate specificity of the two immobilized enzyme samples differed by an order of magnitude. Moreover, EPR spectroscopy studies and computer graphic analyses of spin labels occupying three defined regions of the active-site domain indicated that the active-site conformation adjacent to the catalytic zinc atom was similar in the two samples while the conformation slightly further from the zinc atom was different. This result may explain why the two immobilized enzyme preparations exhibited the same rate constant toward a small substrate (ethanol) yet different rate constants toward a larger substrate (cyclohexanol), whose rate constant is expected to be sensitive to a larger portion of the active site.     

Estimation of intrinsic kinetic constants for pore diffusion-limited immobilized enzyme reactions

A simple method is presented that establishes intrinsic rate parameters when slow pore diffusion of substrate limits immobilized enzyme reactions that obey Michaelis-Menten kinetics. The Aris-Bischoff modulus is employed. Data at high substrate concentrations, where the enzyme would be saturated in the absence of diffusion limitation, and at low substrate concentrations, where effectiveness factors are inversely proportional to reaction modulus, are used to determine maximum rate and Michaelis constant, respectively. Because Michaelis-Menten and Langmuir-Hinshelwood kinetics are formally identical, this method may be used to estimate intrinsic rate parameters of many heterogeneous catalysts. The technique is demonstrated using experimental data from the hydrolysis of maize dextrin with diffusion-limited immobilized glucoamylase. This system yields a Michaelis constant of 0.14%, compared to 0.11% for soluble glucoamylase and 0.24% for immobilized glucoamylase free of diffusional effects.     

Analysis of the transient response of a CSTR containing immobilized enzyme particles: Part I. Model development and analysis of the influence of operating conditions and process parameters

The transient response of the bulk substrate concentration in a CSTR containing immobilized enzyme (IMEs) in porous solid supports and the possibilities of exploiting the minimum behavior for parameter estimation purposes are studied in this work. For that purpose, mathematical models have been developed for several kinetic expressions with parallel deactivation mechanisms and for two different particle shapes (cylindrical and spherical). The influence of a number of system variables and non-dimensional parameters, i.e., pellet radius, mass of particles, flow rate, effective diffusivity, mass transfer coefficient, Thiele modulus, Michaelis constant, and enzyme deactivation constant, is also reported in a systematic way. Simulations, using realistic data, show that the minimum bulk substrate concentration is sufficiently pronounced and the time scale for the minimum to occur is sufficiently practical, so that it can be used to extract several parameters of the immobilized enzyme system.     

Maltodextrin hydrolysis in a fluidized-bed immobilized enzyme reactor

The present work deals with maltodextrin hydrolysis by glucoamylase immobilized onto corn stover in a fluidized bed reactor. An industrial enzyme preparation was covalently grafted onto corn stover, yielding an activity of up to 372 U/g and 1700 U/g for support particle sizes of 0.8 and 0.2 mm, respectively. A detailed kinetic study, using a differential reactor, allowed the characterization of the influence of mass transfer resistance on the reaction catalyzed by immobilized glucoamylase. A simple and general mathematical model was then developed to describe the experimental conversion data and found to be valid.     

Immobilization of lipase from Candida rugosa on a polymer support

Lipase from Candida rugosa was immobilized by adsorption onto a macroporous copolymer support. Under optimum conditions the maximum amount of protein bound was 15.4 mg/g and the immobilization efficiency was 62%. The kinetics of lipase binding to the selected polymer carrier was assessed by using a general model of topochemical reactions. The effect of temperature on adsorption was thoroughly investigated, as was the adsorption mechanism itself. Analysis of the proposed kinetic model and the specific kinetic parameters measured suggest that surface kinetics control the adsorption process. According to the activation energy (E _a) and the rate constant, k, the enzyme has rather a high affinity for the support's active sites. The immobilized enzyme was used to catalyse the hydrolysis of palm oil in a lecithin/isooctane reaction system, in which the enzyme's activity was 70% that of the free enzyme. Kinetic parameters such as maximum velocity (V _max) and the Michaelis constant (K _m) were determined for the free and the immobilized lipase. Following repeated use, the immobilized lipase retained 56% of its initial activity after the fifth hydrolysis cycle. Received: 3 April 1998 / Received revision: 28 July 1998 / Accepted: 29 July 1998     

Determination of the intrinsic kinetic constants of immobilized glucose oxidase and catalase

Models of membrane systems containing immobilized glucose oxidase and catalase operating together or independently have been developed. A rotated disk electrode apparatus was employed with novel electrochemical operating conditions to experimentally determine mass transfer and intrinsic kinetic parameters of enzyme-containing membranes. The value of a mass transfer parameter that describes internal and external diffusion was first determined under conditions that do not permit the enzyme reactions. In a subsequent experiment with the reaction allowed, kinetic parameters corresponding to the intrinsic maximal velocity and Michaelis constants of the immobilized enzymes were estimated by regression analysis of data based on an appropriate two- or three- parameter model. It was found that immobilization reduced the maximal intrinsic velocity but had no detectable effect on the Michaelis constants. In all but one case- these methods for membrane characterization are nondestructive and can be used repeatedly on a given membrane. These techniques provide the means for quantitative comparisons of immobilization methods and make possible temporal studies of immobilized enzyme inactivation.     

Immobilization of enzymes on activated carbon: Properties of immobilized glucoamylase,glucose oxidase,and gluconolactonase

Apparent kinetics and pH–activity relationships have been determined for glucoamylase and glucose oxidase immobilized on activated carbon using a diimide method. Reaction rate expressions of Michaelis–Menten form adequately approximate the observed kinetics for both enzyme preparations over the ranges of substrate concentrations considered. Influences of external mass transfer as well as substrate and product adsorption on interpretation of the experimental data have been examined. Immobilization of a glucose oxidase–gluconolactonase enzyme mixture has been found to increase substantially the ratio of gluconolactonase to glucose oxidase activities compared to the corresponding activity ratio for these enzymes in solution.     

Kinetic analysis of enzymatic hydrolysis of crystalline cellulose by cellobiohydrolase using an amperometric biosensor

An amperometric biosensor for the detection of cellobiose has been introduced to study the kinetics of enzymatic hydrolysis of crystalline cellulose by cellobiohydrolase. By use of a sensor in which pyrroloquinoline quinone-dependent glucose dehydrogenase was immobilized on the surface of electrode, direct and continuous observation of the hydrolysis can be achieved even in a thick cellulose suspension. The steady-state rate of the hydrolysis increased with increasing concentrations of the enzyme to approach a saturation value and was proportional to the amount of the substrate. The experimental results can be explained well by the rate equations derived from a three-step mechanism consisting of the adsorption of the free enzyme onto the surface of the substrate, the reaction of the adsorbed enzyme with the substrate, and the liberation of the product. The catalytic constant of the adsorbed enzyme was determined to be 0.044+/-0.011s(-1).     

Invertase reversibly immobilized onto polyethylenimine-grafted poly(GMA–MMA) beads for sucrose hydrolysis

The epoxy group containing poly(glycidyl methacrylate-co-methylmethacrylate) poly(GMA–MMA) beads were prepared by suspension polymerisation and the beads surface were grafted with polyethylenimine (PEI). The PEI-grafted beads were then used for invertase immobilization via adsorption. The immobilization of enzyme onto the poly(GMA–MMA)–PEI beads from aqueous solutions containing different amounts of invertase at different pH was investigated in a batch system. The maximum invertase immobilization capacity of the poly(GMA–MMA)–PEI beads was about 52 mg/g. It was shown that the relative activity of immobilized invertase was higher then that of the free enzyme over broader pH and temperature ranges. The Michaelis constant (K_m) and the maximum rate of reaction (V_max) were calculated from the Lineweaver–Burk plot. The K_m and V_max values of the immobilized invertase were larger than those of the free enzyme. The immobilized enzyme had a long-storage stability (only 6% activity decrease in 2 months) when the immobilized enzyme preparation was dried and stored at 4 °C while under wet condition 43% activity decrease was observed in the same period. After inactivation of enzyme, the poly(GMA–MMA)–PEI beads can be easily regenerated and reloaded with the enzyme for repeated use.     

Lipoprotein lipase immobilization onto polyacrolein microspheres

A lipoprotein lipase (LPL) was made water insoluble by immobilizing onto the surface of polyacrolein (PAA) microspheres with and without oligoglycines as spacer. The activity of the immobilized LPL was found to remain high toward a small ester substrate, p-nitrophenyl laurate (pNPL). The relative activity of the immobilized LPL without spacer decreased gradually with the decreasing surface concentration of the immobilized LPL on the PAA microsphere. On the contrary, the immobilized LPL with oligoglycine spacers gave an almost constant activity for the substrate hydrolysis within the surface concentration region studied and gave a much higher relative activity than that without any spacer. The Michaelis constant K(m) and the maximum reaction velocity V(m) were estimated for the free and the immobilized LPL. The apparent K(m) was larger for the immobilized LPL than for the free one, while V(m) was smaller for the immobilized LPL. The pH, thermal, and storage stabilities of the immobilized LPL were higher than those of the free one. The initial enzymatic activity of the immobilized LPL maintained almost unchanged without any leakage and inactivation of LPL when the batch enzyme reaction was performed repeatedly, indicating the excellent durability of the immobilized LPL.     

Surface effects of solvents in hydrolysis of water-soluble lipids by candidal lipase

In the study of hydrolysis of tributyrin by the lipase of Candida cylindracea, it is shown that initial rates of hydrolysis are directly proportional to the amount of enzyme adsorbed at the substrate-water interface. As a consequence of understanding the role of the physical state of the substrate in aqueous reaction media, it was hypothesized that the inclusion of synthetic (nonsubstrate) surfaces into the reaction media may enhance the hydrolysis rate of simple liquid lipids which are partly soluble in water, like triacetin. Nonpolar n-hydrocarbons having 5-11 carbon atoms were used to create interfaces in the hydrolysis of triacetin in the soluble range. All of the C(5)-C(11) hydrocarbons showed an activating effect. For quantitative evaluation of the effects of n-hydrocarbons, n-heptane was chosen as the model n-hydrocarbon. Interrelations between the reaction kinetics and adsorption of the enzyme at the n-heptane-water interface were experimentally determined by the use of the same in-line filtration device used for the tributyrin-water system. At 35 degrees C and pH 6 the relative values of the rate constants for the decomposition of enzyme-interface-substrate complexes were calculated as 12 and 1 for the tributyrin and n-heptane-triacetin systems, respectively. The nature of activation at the solvent surfaces were accounted for by a kinetic model which assumes simultaneous adsorption of enzyme and triacetin molecules at the n-heptane-water interface. Making use of the proposed model, the value of a the apparent Michaelis constant for the soluble triacetin-n-heptane system at constant n-heptane concentration, 2 vol %, was calculated as 0.044 mol/L.     

Studies of substrate-induced conformational changes in human cytomegalovirus protease using optical biosensor technology

The interaction between human cytomegalovirus (HCMV) protease and a peptide substrate was studied using a surface plasmon resonance (SPR)-based biosensor. Immobilization of the enzyme to the sensor chip surface by amine coupling resulted in an active enzyme with a higher catalytic efficiency than the enzyme in solution, primarily due to a lower K(m) value. The interaction between immobilized protease and substrate was characterized by a biphasic SPR signal. Rate constants for the formation of the initial enzyme-substrate complex could be determined from the sensorgrams. Simulated binding curves based on the determined k(cat) and the rate constants indicated that the complex binding signal did not originate from the accumulation of intermediates in the catalytic reaction. By chemical crosslinking of the immobilized HCMV protease, which was shown to limit the enzyme's structural flexibility, it was revealed that the obtained sensorgrams were composed of a signal caused by substrate binding and considerable structural alterations in the immobilized enzyme. Furthermore, HCMV protease was inactivated by chemical crosslinking, indicating that structural flexibility is essential for this enzyme. Parallel experiments with immobilized alpha-chymotrypsin revealed that it does not undergo similar conformational changes on peptide binding and that crosslinking did not inactivate the enzyme. The simultaneous detection of binding and conformational changes using optical biosensor technology is expected to be of importance for further characterization of the enzymatic properties of HCMV protease and for identification of inhibitors of this enzyme. It can also be of use for studies of other flexible proteins.     

Preparation and characterization of kappa-carrageenan immobilized urease

Urease was encapsulated within kappa-carrageenan beads. Various parameters, such as amount of kappa-carrageenan and enzyme activity, were optimized for the immobilization of urease. Immobilized urease was thoroughly characterized for pH, temperature, and storage stabilities and these properties were compared with the free enzyme. The free urease activity quickly decreased and the half time of the activity decay was about 3 days at 4 degrees C. The immobilized urease remained very active over a long period of time and this enzyme lost about 70.43% of its orginal activity over the period of 26 days for storage at 4 degrees C. The Michaelis constant (Km) and maximum reaction velocity (Vmax) were calculated from Lineweaver-Burk plots for both free and immobilized enzyme systems. Vmax = 227.3 U/mg protein, Km = 65.6 mM for free urease and Vmax = 153.9 U/mg protein, Km = 96.42 mM for immobilized urease showed a moderate decrease of enzyme specific activity and change of substrate affinity.     

Direct immobilization of tyrosinase enzyme from natural mushrooms (Agaricus bisporus) on D-sorbitol cinnamic ester

Mushroom tyrosinase was immobilized from an extract onto the totally cinnamoylated derivative of D-sorbitol by direct adsorption as a result of the intense hydrophobic interactions that took place. The immobilization pH value and mass of lyophilized mushrooms were important parameters that affected the immobilization efficiency, while the immobilization time and immobilization support concentration were not important in this respect. The extracted/immobilized enzyme could best be measured above pH 3.5 and the optimum measuring temperature was 55 degrees C. The apparent Michaelis constant using 4-tert-butylcatechol as substrate was 0.38+/-0.02 mM, which was lower than for the soluble enzyme from Sigma (1.41+/-0.20 mM). Immobilization stabilized the extracted enzyme against thermal inactivation and made it less susceptible to activity loss during storage. The operational stability was higher than in the case of the tyrosinase supplied by Sigma and immobilized on the same support. The results show that the use of p-nitrophenol as enzyme-inhibiting substrate during enzyme extraction and immobilization made the use of ascorbic acid unnecessary and is a suitable method for extracting and immobilizing the tyrosinase enzyme, providing good enzymatic activity and stability.     

Numerical simulation and deacidification of nanomagnetic enzyme conjugate in a liquid–solid magnetic fluidized bed

The conventional deacidification method is difficult to achieve a better refining effect due to the high acid value in the rice bran crude oil, and the enzymatic esterification deacidification method can effectively reduce the acid value without generating chemical waste. In this study, the free lipase was immobilized on a magnetic polymer carrier Fe₃O₄/SiOx-g-P (GMA: glycidyl methacrylate) to obtain a immobilized lipase with a particle size of 105.30 ± 1.1 nm and an enzyme activity of 6580 ± 9.6 PLU/g (PLU: enzyme activity unit). Based on the batch deacidification process parameters, a multi-stage magnetic fluidized bed continuous circulation deacidification system was designed, and then the motion law of nanomagnetic immobilized lipase particles in liquid–solid magnetic fluidized bed was simulated by computer. When the iterative step was 5 × 10⁻⁵ s, the open porosity of the porous plate was 35.0%, the rice bran oil flow rate was 3.0 mm/s, and the magnetic field strength was 25.0 mT, which was beneficial to the deacidification reaction of rice bran oil. Under the conditions of magnetic immobilized lipase dosage of 4.0%, the phytosterol dosage of 22.0%, the molecular sieve dosage of 10%, the esterification temperature of 78.0 °C and the FFA (free fatty acid) content in rice bran oil decreased to 1.5%, after 48 h of reaction. The conversion rate is 92.8%, which provides a theoretical basis for the subsequent guidance of magnetic fluidized bed enzymatic continuous deacidification.