Characteristics of yeast invertase immobilized on porous cellulose beads.

Invertase from Candida utilis was immobilized on porous cellulose beads by an ionic-quanidino bond. The immobilized invertase showed optimum activity between pH 4.0 and 5.4, while the free enzyme had a sharp optimum at pH 4.1. Both temperature profiles were fairly similar up to 55 degrees C. However, above this temperature the immobilized enzyme was more stable than the free enzyme. From the temperature data, the activation energies were found to be 7,322 and 4,052 cal/g mol for the free and the immobilized enzyme, respectively. Candida invertase shows characteristics of substrate inhibition. Both the Km and Ki for the free and the immobilized enzymes were determined. The apparent Ki for the immobilized invertase was much higher than the Ki of the free enzyme, suggesting a diffusion effect. Immobilized invertase molecules deep in the pores only see sucrose concentrations much less than the bulk concentrations. Immobilization, thus, offers certain processing advantages in this regard.     

A batch reactor mass transfer kinetic model for immobilized biomass biosorption

Inactive cells of Rhizopus arrhizus have been immobilized into the form of particles of desirable particle size using a proprietary immobilization technique. The immobilized biomass particles are porous and are members of a new generation of biological origin adsorbents. The uranium adsorptive behavior of the biosorbent particles was modeled using a batch reactor mass transfer kinetic model of the biosorption process. The model successfully predicts the batch reactor adsorbate (uranium) concentration profiles and has provided significant insights on the way biosorbents function.     

Enzyme immobilized in a packed-bed reactor: kinetic parameters and mass transfer effects.

To describe axial dispersion, particle film mass transfer, intraparticle diffusion, and the chemical reaction of the substrate for enzymes immobilized in porous particles in packed columns, we have developed mathematical models for first- and zero-order limits of Michaelis-Menten kinetics. Steady-state solutions were derived for both long and short column boundary conditions and for plug flow. Theory was compared to experiments by hydrolysis of sucrose catalyzed by invertase bound to porous glass particles. Steady-state conversions were measured for a range of flow rates. Pulse response experiments with inert packing were used to determine values of bed void fraction and particle porosity.     

Preparation of immobilized invertase

Immobilized invertase was prepared by ionically binding the enzyme to diethylaminoacetyl cellulose (DEAA-cellulose). DEAA-cellulose-invertase complex was quite stable to electrolyte in the range of pH 5–7. Bound invertase was less active than the native enzyme, and approximately 55–70% of the enzyme activity was lost on binding. The complex was stable for 9 days' continuous inversion in a column system at 30°C, but was rather unstable at 40°C. Heat stability and the effect of temperature on the reaction rate of the complex were almost identical with those of the native enzyme.     

Characteristics of immobilized invertase

Five kinds of immobilized invertases (IMI)—covalently of porous glass and ion-exchange resins and ionically on ion-exchange resins—have been prepared and their kinetic characteristics for sucrose hydrolysis, such as K_m, K, pH profile, and thermal stability were studied. Comparing the values of K_m and activation energy and the entropy of IMI with those of native invertase, it was concluded that the immobilization influences not binding but kinetic specificity. The effects of the immobilization method on thermal stability were also discussed.     

Preparation and kinetic behavior of immobilized whole cell biocatalysts

Actinoplanes missouriensis (for glucose isomerase), Kluyveromyces fragilis (for beta-galactosidase), and Saccharomyces cerevisiae (for invertase) cells were successfully entrapped within cellulose and cellulose di- and triacetate beads employing several carried solvent systems. Cellulose beads prepared using a melt of dimethylsulfoxide (DMSO) and N-ethylpyridinium chloride (NEPC), or cellulose diacetate using a mixture of acetone and DMSO as solvent, were found to be promising as carriers for the invertase system, cellulose triacetate beads with DMSO as solvent for yeast beta-galactosidase, and cellulose beads with a melt of DMSO and NEPC as solvent for glucose isomerase. The kinetic behavior of A. missouriensis glucose isomerase whole cell cellulose beads in a plug-flow column reactor was studied as an example system in greater detail.     

Mass transfer limitations in gel beads containing growing immobilized cells

Immobilized-cell aggregates have traditionally been approximated as effective continua within which the catalytic activity of the cells is homogeneously distributed. Chang & Park (1985), however, recently modelled the immobilized cells as discrete inclusions within a support matrix. With some modification, this theory is applicable to the analysis of microbial colonies growing within gel beads, and indicates that predictions obtained using the traditional approach may be significantly in error.     

Kinetic study on thermal stability of immobilized invertase

The kinetic study of the thermal stability of three kinds of invertases: native, immobilized on porous glass covalently, and on ion-exchange resin ionically, has been carried out, measuring their enzymatic activity for sucrose hydrolysis. Thermal deactivations of all invertases obeyed first-order kinetics, being independent of substrate concentration, with k_d and ΔE_d, ΔS_d* as shown in Tables I and II, respectively. Based on these parameter values, the effects of immobilization and pH at deactivation on the stability have been considered, and it was suggested that the ionic bond gives a more loosely deformed enzyme than the covalent bond.     

Impact of denaturation with urea on recombinant apolipoprotein A-IMilano ion-exchange adsorption: equilibrium uptake behavior and protein mass transfer kinetics

We have studied the equilibrium uptake behavior and mass transfer rate of recombinant apolipoprotein A-I(Milano) (apo A-I(M)) on Q Sepharose HP under non-denaturing, partially denaturing, and fully denaturing conditions. The protein of interest in this study is composed of amphipathic alpha helices that serve to solubilize and transport lipids. The dual nature of this molecule leads to the formation of micellar-like structures and self association in solution. Under non-denaturing conditions equilibrium uptake is 134 mg/mL media and the isotherm is essentially rectangular. When fully denatured with 6 M urea, the equilibrium binding capacity decreases to 25 mg/mL media and the isotherm becomes less favorable. The decrease in both binding affinity and media capacity when the protein is completely denatured with 6 M urea can be explained by the loss of all alpha helical structure. The rate of apo A-I(M) mass transfer on Q Sepharose HP was characterized using a macropore diffusion model. Results of modeling studies indicate that effective pore diffusivity increases from 4.5 x 10(-9) cm2/s in the absence of urea to 6.0 x 10(-8) cm2/s when apo A-I(M) is fully denatured with 6 M urea. Based on light-scattering data reported for apo A-I, protein self association appears to be the dominant cause of slow protein mass transfer observed under non-denaturing conditions.     

Sucrose hydrolysis using invertase immobilized on concanavalin A-sepharose

The stability and ability of yeast invertase (β-d-fructofuranoside fructohydrolase, EC 3.2.1.26) bound and covalently coupled to concanavalin A-Sepharose continuously to hydrolyse sucrose over long periods has been investigated. The immobilized preparation exhibited high resistance to heat and urea induced denaturation. A small column of the immobilized preparation could hydrolyse relatively high concentrations of sucrose almost quantitatively for more than 60 days.     

Biosorption behavior of azo dye by inactive CMC immobilized Aspergillus fumigatus beads

The biosorption equilibria and kinetics of an azo dye (reactive brilliant red K-2BP) were examined in this study using inactive carboxylmethylcellulose (CMC) immobilized Aspergillus fumigatus beads as the biosorbent. It was found that the biosorption capacity was at maximum when dye solution pH was about 2.0, that the sorption was spontaneous and endothermic with insignificant entropy changes, and that the Freundlich isotherm model fitted well to the biosorption equilibrium data. The biosorption rates were found to be consistent with a pseudo-second-order model. An intraparticle diffusion-based Weber-Morris model was applied to evaluate rate-limiting steps of the biosorption processes. The results suggested that the diffusion controlled the overall biosorption process, but the boundary layer diffusion of dye molecules could not be neglected. External mass transfer coefficients (beta(I)S) obtained by both Mathews and Weber model and Frusawa and Smith model were consistent.     

The properties of invertase,covalently immobilized at activated carbon

The covalent immobilization of yeast invertase with glutaraldehyde at activated carbon, modified preliminarily by urea and dimethyl formamide treatment, has been established. Some physicochemical properties of the immobilized and native enzyme in water and water-organic solutions have been studied. Hydrolytic, as well as transferase enzyme characteristics have changed after immobilization. The optimal conditions for hydrolytic and transferase activity of immobilized invertase are pH 6.0 and 7.0, respectively. The optimum temperature for the immobilized enzyme is 30°C. The conversion degree of isoamyl alcohol depends on the substrate and enzyme concentrations in medium, holdup time and organic phase quantity in the reaction medium.     

Electron transfer between soluble and immobilized mammalian cytochrome c. Equilibrium and kinetic studies on immobilized cytochrome c.

Horse heart cytochrome c was covalently bound to Sepharose 4B and its redox properties were measured under various experimental conditions. The equilibrium constant for the electron exchange between the oxidized and the reduced form of cytochrome c when one of the two forms was in the semi-solid state and the other one in solution was close to 1. Matrix-bound ferrocytochrome c is very stable to autoxidation and is not oxidized by O2 even in the presence of mammalian cytochrome oxidase. Oxidation occurs if catalytic amounts of soluble cytochrome c are added to the reaction mixture. The rate of oxidation of matrix-bound ferrocytochrome c in the presence of cytochrome oxidase and catalytic amounts of soluble cytochrome c may be correlated with the rate of electron transfer between soluble and matrix-bound cytochrome c. This rate is more than two orders of magnitude lower than that reported for the homonuclear (between identical species) electron transfer in solution.     

Conjugal transfer of plasmid DNA between streptococci immobilized in calcium alginate gel beads

A rapid and simple technique was developed for conjugation between group N and group D streptococci by using cells entrapped within calcium alginate gel beads. With this method, the frequencies of transfer of lactose metabolism from Streptococcus lactis ME2 to S. lactis LM2302 were comparable to those achieved with agar surface matings. Conjugal transfer of the chloramphenicol and erythromycin resistance plasmid pVA797::Tn917 from S. faecalis V1229 to S. faecalis V1102 in alginate beads occurred at frequencies comparable to those achieved with filter matings. The results demonstrated efficient conjugal transfer of plasmid DNA among alginate-immobilized streptococcal cells and suggested that this method could be used as an alternative to conventional solid-surface and filter matings with these organisms.     

Sucrose hydrolysis by invertase immobilized on functionalized porous silicon

A successful recipe for the production of immobilized invertase/porous silicon layer with appropriate catalytic behavior for the sucrose hydrolysis reaction is presented. The procedure is based on support surface chemical oxidation, silanization, activation with glutaraldehyde and finally covalent bonding of the free enzyme to the functionalized surface. The catalytic behavior of the composite layer as a function of pH, temperature, and the current density applied in the porous silicon (PS) preparation is investigated. Interestingly, V_max undergoes a substantial increase (ca. 30%) upon immobilization. The value of K_m increases by a factor of 1.53 upon immobilization. The initial activity is still preserved up to 28 days while the free enzyme undergoes a 26% loss of activity after the same period. Based on the outcomes of this study, we believe that tailored PS layers may be used for the development of new bioreactors in which the active enzyme is immobilized on the internal walls and is not lost during the process.     

The preparation and properties of hornblende as a support for immobilized invertase

The suitability of hornblende as a support for immobilized β-fructofuranosidase (invertase) was studied, with regard to the physical stability of the support and the thermal and operational stability of the immobilized enzyme. Hornblende was more stable than Enzacryl-Alo or Enzacryl-TIO, and marginally more stable than porous glass. Invertase immobilized on hornblende was more stable during long-term operation than invertase immobilized on porous glass. An active preparation of immobilized invertase was obtained also on pyroxene particles.     

New approaches for verification of kinetic parameters of immobilized concanavalin A: invertase preparations investigated by flow microcalorimetry

In our preceding article, we demonstrated a procedure based upon enzymic flow microcalorimetry using an enzyme thermistor (ET) to characterize the microkinetic properties of an immobilized enzyme (IME) and its further application in the screening of IMEs. To consider the ET method (single ET unit, ET system 1) as standard, it was necessary to show that the estimated relative kinetic parameter (DeltaT(max)) calorimetrically corresponds with the absolute value for the reaction rate within the whole measurement range. This article presents three experimental verification procedures. Two procedures are based on adaptation of the flow-through ET column to a mini-differential-reactor (DR) system with substrate recirculation and post-ET-column methods for determination of the concentration change of the product (spectrophotometrically in ET system 2) or the substrate (calorimetrically in ET system 3) with the IME-catalyzed enzymic hydrolysis. The third procedure is an independently operating DR system which spectrophotometrically estimates the concentration change of the product. The results obtained exhibited good correlation (r = 0.921) between the relative kinetic parameter DeltaT(max), as determined calorimetrically by ET system 1, and the absolute value for the reaction rate (r(max)) as determined by ET systems 2 and 3. These data proved that, within the whole range of experimental conditions applied in this study, the parameter DeltaT(max) instead of the true reaction rate could be employed for the IME screening. Moreover, the generality of the detection principle and the standardized configuration of the ET favor ET systems 2 and 3 for normal screening of IMEs and as miniaturized DR systems allowing dual measurements of kinetic parameters. (c) 1996 John Wiley & Sons, Inc.     

Distribution of saccharides and salts on amphoteric ion-exchange resin

An amphoteric ion-exchange resin hardly shrank in 550 and 300 g/L glucose and sodium chloride solutions, respectively; however, the bed packed with a cation-exchange resin shrank considerably. From the distribution coefficients of some saccharides, the swelling pressure of the amphoteric ion-exchange resin was estimated to be 2.0 MPa at 25 °C. The distribution coefficients of glucose, galactose, fructose, and mannose were independent of their concentration and were about 0.621. On the other hand, the apparent distribution coefficients of NaF, NaCl, NaBr, NaI, LiCl, KCl, and CsCl largely depended on concentration. A model for the distribution of salts on the amphoteric resin was proposed, assuming an interaction between the anion of the salt and the positively charged fixed ions with binding constant B. The B values of the chloride salts were nearly the same (1.69–2.94 L/mol), while the values of the sodium salts were largely different depending on the anion.