Enzyme inactivation and stabilization studies in an ultrafiltration reactor

Summary An ultrafiltration membrane enzymatic reactor is used in connection with different reacting systems.The experimental conditions are such that the enzyme, which operates at fairly high concentration levels because of the concentration polarization phenomena taking place in the reactor, is still in soluble form.The analysis of the system unsteady-state response enables the identification of the mechanism of enzyme deactivation and the extraction of the kinetic parameters of both the deactivation and the main reaction.The stabilizing effect observed in connection with enzyme entrapment within an inert gel deposited onto the U.F. membrane active surface is also discussed.List of Symbols A U.F. membrane cross sectional area cm² - C_E Enzyme concentration mg/ml - C_EI Enzyme concentration at the active membrane surface mg/ml - C_E Mean enzyme concentration mg/ml - c _s ^o Substrate concentration in the feed m moles/ml - c _s ^u Substrate concentration in the outlet m moles/ml - D_E Enzyme diffusivity cm²/s - Km michaelis constant mM - k₂ Kinetic constant of the enzymatic reaction m moles/mg s - k_d Kinetic constant of the enzyme deactivation reaction s^–1 - N^o Initial amount of active enzyme mg - N(t) Active enzyme amount at reaction time t mg - Q Flow rate ml/s - r Rate of the main reaction m moles/ml s - t Reaction time s - t^* Reaction time at which product concentration in the outlet is within ± 2% of the steady-state value s - v Fluid velocity cm/s - V Cell volume ml - V_B Volume within which 99% of the enzyme fed is contained at the steady-state ml - V_S Volume within which 99% of the total substrate concentration drop occurs at the steady-state ml - x Distance upstream the membrane measured from the membrane surface cm     

Enzyme immobilized reactor design for ammonia removal from waste water

Removal of nitrogen compound from waste, water is essential and often accomplished by biological process. To prevent washout and to develop an efficient bioreactor, immobilization of suitable microorganisms could be sensible approach. Strains and permeabilized cells encapsulated in cellulose nitrate microcapsules and immobilized on polystyrene, films were prepared by the method described in the previous study. In the wastewater, treatment system, nitrification of ammonia component is generally known as rate controlling step. To enhance the rate of nitrification, firstly nitrifying strainsNitrosomonas europaea (IFO 14298), are permeabilized chemically, and immobilized on polystyrene, films and secondly oxidation rates of strain system and permeabilized strain system are compared in the same condition. With 30 minute permeabilized cells, it took about 25 hours to oxidize 70% of ammonia in the solution, while it took about 40 hours to treat same amount of ammonia with untreated cells. All the immobilization procedures did not harm to the enzyme activity and no mass transfer resistance through the capsule wall was shown. In the durability test of immobilized system, the system showed considerable activity for the repeated operation for 90 days. With these results, the system developed in this study showed the possibility to be used in the actual waste water treatment system.     

Temperature optimization for reactor operation with chitin-immobilized lactase under modulated inactivation

Temperature effects on all kinetic and inactivation parameters have been determined for chitin immobilized lactase from Kluyveromyces marxianus var. marxianus, and proper temperature functions have been validated. Maximum reaction rate, Michaelis constant referred to lactose, inhibition constant for galactose and inactivation rates increased with temperature. Enzyme inactivation was adequately modelled by a two-stage series mechanism. The effect of galactose and lactose on enzyme inactivation was determined in terms of modulation factors that were positive for galactose and negative for lactose over the whole range of temperature studied. Modulation factors were mild functions of temperature in the first stage and strong functions in the second stage of CIL inactivation where galactose positive modulation factors increase with temperature and lactose negative modulation factors decrease with temperature. Temperature explicit functions for all kinetic and inactivation parameters were incorporated into a scheme to optimize the temperature of operation for a sequential batch reactor with chitin-immobilized lactase, based on an annual cost objective function for reactor operation. Software for temperature optimization was developed creating a friendly interface with user that allows the introduction of variations in all parameters and operational criteria to perform sensitivity analysis.     

Enzyme inactivation with shearing

Enzymes subjected to shearing in a viscometer are partially inactivated. It is possible with viscometry to calculate the degree of inactivation that occura when an enzyme solution flows through a capillary tube. When shear rate × exposure time is less than 10⁴, there is little or no inactivation. The masa average shear-rate × time or shear, for laminar flow in a cylindrical tube is simply 16L/3D. It is surprising that for a single pass through a tube, the masa average shear is independent of flow rate and shear rate.     

Enzyme inactivation and inhibition by Gossypol

Summary Three lactate dehydrogenase isozymes and malate dehydrogenase purified from mouse tissues were inactivated with time by low concentration of gossypol. The degree of enzyme inactivation is both gossypoland enzyme-concentration-dependent. Under the same experimental conditions, lactate dehydrogenase-X and lactate dehydrogenase-5 were inactivated faster than lactate dehydrogenase-1. NADH was shown to partially protect the enzymes against inactivation by gossypol. The results of this study suggest that the enzymes are inactivated by the minor components in gossypol preparations. Isozymes of glutathione S-transferases were reversibly inhibited by gossypol. The inhibition of transferases by gossypol was shown to be competitive with respect to the 1-chloro-2,4-dinitrobenzene. It is proposed that the male antifertility effect of gossypol may be related to the selective inactivation of sperm-specific lactate dehydrogenase-X.     

Enzyme inactivation after exposure to mechanical factors

Kinetics of decreasing proteolytic activity of subtilisin and trypsin during grinding of powders was studied. The enzymes were ground in a ball laboratory vibromill for 1-80 min within the temperature range 80-300 K in the air or helium. Proteolytic activity of the enzymes measured by the splitting of low molecular p-nitroanilide substrates decreases with the increase of the treatment time according to the equation of the first order. By means of titration of trypsin active centres a decrease of their number after grinding was shown. Kinetic parameters in Michaelis-Menten equation were determined for trypsin enzymic reaction. It was found that the value kappa kat decreased with an increase of the time of mechanical treatment.     

Characteristics of thermal inactivation of malate dehydrogenase

Over the range 20-52 degrees C thermal inactivation of malate dehydrogenase (MDH) was studied with the aim of well grounded choice of its stabilization ways. The process was described by the pseudofirst order rate constants, kin, dependent on enzyme concentration. The rate constant of enzyme inactivation at the "infinite" dilution in general form equals 1.40 X 10(27) X exp (-43 000/RT) s-1, whereas at high enzyme concentration it is 1.26 X 10(8) X exp (-17 700/RT) s-1. The limiting step of the MDH inactivation is the enzyme dissociation into its subunits. In the concentrated enzyme solution a protein association is accompanied by its stabilization. The methods of characterization of oligomeric proteins dissociative inactivation are discussed.     

Experimental modelling of thermal inactivation of urease

Thermal inactivation of jack bean urease (EC 3.5.1.5) was investigated in a 0.1 M phosphate buffer with pH 7. An injection flow calorimetry method was adapted for the measurement of the enzyme activity. The inactivation curves were measured in the temperature range of 55 to 87.5 degrees C. The curves exhibited a biphasic pattern in the whole temperature range and they were well fitted with a biexponential model. A simultaneous fit of all inactivation data was based on kinetic models that were derived from different inactivation mechanisms and comprised the material balances of several enzyme forms and the enthalpy balance characterizing the initial heating period of enzyme solution. The multitemperature evaluation revealed that an adequate model had to incorporate at least three reaction steps. It was concluded that the key reaction steps at urease thermal inactivation were the reversible dissociation/denaturation of native form into an inactive denatured form, and irreversible association reactions of both the denatured and native forms.     

Enzyme inactivation by metal-catalyzed oxidation of coenzyme Q1.

Ubiquinol-1 in aerated aqueous solution inactivates several enzymes--alanine aminotransferase, alkaline phosphatase, Na+/K(+)-ATPase, creatine kinase and glutamine synthetase--but not isocitrate dehydrogenase and malate dehydrogenase. Ubiquinone-1 and/or H2O2 do not affect the activity of alkaline phosphatase and glutamine synthetase chosen as model enzymes. Dioxygen and transition metal ions, even if in trace amounts, are essential for the enzyme inactivation, which indeed does not occur under argon atmosphere or in the presence of metal chelators. Supplementation with redox-active metal ions (Fe3+ or Cu2+), moreover, potentiates alkaline phosphatase inactivation. Since catalase and peroxidase protect while superoxide dismutase does not, hydrogen peroxide rather than superoxide anion seems to be involved in the inactivation mechanism through which oxygen active species (hydroxyl radical or any other equivalent species) are produced via a modified Haber-Weiss cycle, triggered by metal-catalyzed oxidation of ubiquinol-1. The lack of efficiency of radical scavengers and the almost complete protection afforded by enzyme substrates and metal cofactors indicate a 'site-specific' radical attack as responsible for the oxidative damage.     

Studies on the thermal inactivation of immobilized enzymes

The thermal inactivation of a great number of immobilized enzymes shows a biphasic kinetics, which distinctly differs from the first-order inactivation kinetics of the corresponding soluble enzymes. As shown for alpha-amylase, chymotrypsin, and trypsin covalently bound to silica, polystyrene, or polyacrylamide, the dependence of the remaining activities on the heating time can be well described by the sum of two exponential terms. To interpret this mathematical model function, the catalytic properties of immobilized enzymes (number of active sites in silica-bound trypsin, K(M) and E(a) values in silica-bound alpha-amylase and chymotrypsin) at different stages of inactivation and the influence of various factors (coupling conditions, addition of denaturants or stabilizers, etc.) on the thermal inactivation of silica-bound alpha-amylase were studied. Furthermore, conformational alterations in the thermal denaturation of spin-labeled soluble and silica-bound beta-amylase were compared by electron spin resonance (ESR) studies. The results suggest that the biphasic inactivation kinetics reflects two different pathways according to which catalytically identical enzyme molecules are predominantly inactivated.     

Sorbitol-mediated stabilization of human IgG against thermal inactivation

Sorbitol at 30% (w/w) stabilized human IgG to thermal denaturation from 60 to 85°C, increasing the protein's half life from 25 to 266 min at 70°C. A kinetic model based on the Lumry-Eyring inactivation scheme was developed and used to estimate the apparent rate constant and activation energy. © Rapid Science. 1998     

Optimizing thermal and radiation effects for bacterial inactivation

The temperatures required for dry-heat spacecraft sterilization have been known to degrade heat-sensitive components. Thermoradiation, the simultaneous application of dry heat and gamma radiation, can provide the same degree of microbial inactivation as dry heat alone while substantially reducing component degradation. This is made possible by the synergistic effects produced when relatively low levels of these agents (e.g., 90 to 350 krads and 60° to 105°C) are applied simultaneously, thus permitting the use of lower temperatures and a reduced duration of heat exposure. The effects of temperature, radiation dose rate, and relative humidity on microbial inactivation during thermoradiation exposure have been established.This experimentation was supported by NASA Contract No. W-12853.     

Mechanisms of irreversible thermal inactivation of Bacillus alpha-amylases

Molecular mechanisms of irreversible thermal inactivation of two bacterial alpha-amylases, from the mesophile Bacillus amyloliquefaciens and from the thermophile Bacillus stearothermophilus, have been elucidated in the pH range of relevance to enzymatic catalysis. At pH 5.0, 6.5, and 8.0, B. amyloliquefaciens alpha-amylase irreversibly inactivates due to a monomolecular conformational process, formation of incorrect (scrambled) structures which subsequently undergo aggregation. At the last pH, this process can be suppressed by the presence of the substrate starch and consequently a covalent process, deamidation of asparagine and/or glutamine residues, becomes the cause of loss of enzymatic activity at 90 degrees C. Monomolecular conformational scrambling is the predominant cause of irreversible inactivation of B. stearothermophilus alpha-amylase at 90 degrees C at pH 5.0, 6.5, and 8.0. At pH 6.5 another contributing inactivation mechanism is the deamidation of amide residues, and at pH 8.0, O2 oxidation of the enzyme's cysteine residue.     

Characteristics of thermal inactivation of lysozyme in solution

In the buffer solution (pH 6,2) at 20-80 degrees, the lysozyme thermoinactivation was studied by monitoring of its activity decrease in the lysis of M. lysodeicticus cells. Protein inactivation was characterized by effective pseudofirst order rate constants which depend on enzyme concentration and are described by equation k = k0 . exp [-alpha 0 (1-gamma/T) [E]0], where k0 is inactivation rate constant at "infinite" enzyme dilution, [E0] is an initial lysozyme concentration, alpha 0 and gamma are the coefficients independent on [E0]. By extrapolation of the "k" dependencies on [E]0 the constants k0 were determined. In the range 40-70 degrees C, the rate constant k0 is equal 4,0 X 10(11) . exp (-24 200/RT) sec-1.     

Evaluation of microfluidics reactor technology on the kinetics of virus inactivation

Mammalian cell lines constitute an important part in the manufacture of therapeutic proteins. However, their susceptibility to virus contamination is a potential risk to patient safety and productivity, and has led to the development of a repertoire of virus inactivation techniques. From a process development viewpoint, the challenge is to demonstrate the required log reduction in virus content without a significant loss in product titer or quality. The balance between the two is dictated by the kinetics of virus inactivation and protein degradation, both of which are critically affected by process parameters. In this study we describe a commercially available microchannel reactor (MCR) and demonstrate how it can be used to evaluate the impact of temperature on the kinetics of virus inactivation and protein product degradation. Virus spiking experiments are reported using Xenotropic Murine Leukemia Virus and REOvirus, into buffers in the absence and presence of a therapeutic protein currently under development at Lilly. The results demonstrate that the MCR is an ideal platform for evaluation of fast reactive systems and reactions that are particularly sensitive to small changes to process conditions. These conditions include heat inactivation of a virus in a mammalian cell culture process stream used in the manufacture of therapeutic proteins and antibodies.     

Enzyme models: design and selection

There are two approaches to the discovery of enzyme mimics, that is identifying molecules that are able to bind substrate(s) and then catalyze reactions. The first approach, often inspired by enzymes themselves, utilises chemical knowledge and experience to design the catalyst. The other approach is to create a library and select the best host of a transition state analogue of the required reaction.