Valentina Grano

The influence of the support nature on the kinetics parameters, inhibition constants and reactivation of immobilized acetylcholinesterase

Acetylcholinesterase (AChE) was immobilized on two different composite membranes constituted by a chemically modified poly-acrylonitrile (PAN) membrane plus a layer of tethered chitosan of different molecular weight, 10 kDa or 400 kDa. AChE was also directly immobilized on a chemically modified PAN membrane with NaOH and ethylenediamine (EDA) without chitosan. To know how the different supports affected the enzyme activity and the kinetic parameters, the AChE activity was studied in the soluble form and in the insoluble form with all the three types of modified PAN membranes. The best performance was obtained by the modified PAN membrane having the chitosan with the lower molecular weight. The results concerning the AChE inhibition by methyl-paraoxon and the subsequent reactivation by pyridine-2-aldoxime methochloride (2-PAM) are presented and discussed. The composite membrane having chitosan with the lower molecular weight appeared to be potentially useful for applications in the field of biosensors.

Nonisothermal Bioreactors in the Treatment of Vegetation Waters from Olive Oil: Laccase versus Syringic Acid as Bioremediation Model

Laccase from Trametes versicolor was immobilized by diazotization on a nylon membrane grafted with glycidil methacrylate, using phenylenediamine as spacer and coupling agent. The behavior of these enzyme derivatives was studied under isothermal and nonisothermal conditions by using syringic acid as substrate, in view of the employment of these membranes in processes of detoxification of vegetation waters from olive oil mills. The pH and temperature dependence of catalytic activity under isothermal conditions has shown that these membranes can be usefully employed under extreme pH and temperatures. When employed under nonisothermal conditions, the membranes exhibited an increase of catalytic activity linearly proportional to the applied transmembrane temperature difference. Percentage activity increases ranging from 62% to 18% were found in the range of syringic acid concentration from 0.02 to 0.8 mM, when a difference of 1°C was applied across the catalytic membrane. Because the percentage activity increase is strictly related to the reduction of the production times, the technology of nonisothermal bioreactors has been demonstrated to be an useful tool also in the treatment of vegetation waters from olive oil mills.

Urea removal from agricultural waste waters by means of urease immobilized on nylon membranes grafted with cyclohexyl-methacrylate

Abstract In view of the treatment of agricultural waste waters, urea polluted, a catalytic and hydrophobic membrane was constructed by immobilizing urease on a nylon sheet grafted with cyclohexyl methacrylate (CHMA). Hexamethylenediamine (HMDA) and glutaraldehyde (GA) were used as spacer and crosslinking agent, respectively. With reference to the soluble counterpart immobilized urease was found to exhibit (i) a shift of the optimum pH towards more acidic values; (ii) a shift of the optimum temperature towards higher temperatures; (iii) higher values of Km. The latter result indicated an apparent loss of affinity of immobilized urease towards urea. To recovery this affinity loss, the catalytic membranes were employed in a bioreactor operating under non-isothermal conditions. Under these conditions the catalytic membranes exhibited reaction rates higher and apparent Km smaller than those measured under comparable isothermal conditions. As a consequence, percentage increases of enzyme activity and reduction of the production times, proportional to the magnitude of the applied temperature difference were observed. Results have been discussed in the frame of reference of the process of thermodialysis. The technology of the non-isothermal bioreactors confirmed its usefulness also in the reduction of urea concentration in aqueous solutions.

Apple Juice Clarification by Immobilized Pectolytic Enzymes in Packed or Fluidized Bed Reactors

The catalytic behavior of a mixture of pectic enzymes, covalently immobilized on different supports (glass microspheres, nylon 6/6 pellets, and PAN beads), was analyzed with a pectin aqueous solution that simulates apple juice. The following parameters were investigated: the rate constant at which pectin hydrolysis is conducted, the time (tau(50)) in which the reduction of 50% of the initial viscosity is reached, and the time (tau(comp,dep)) required to obtain complete depectinization. The best catalytic system was proven to be PAN beads, and their pH and temperature behavior were determined. The yields of two bed reactors, packed or fluidized, using the catalytic PAN beads, were compared to the circulation flow rate of real apple juice. The experimental conditions were as follows: pH 4.0, T = 50 degrees C, and beads volume = 20 cm(3). The initial pectin concentration was the one that was present in our apple juice sample. No differences were observed at low circulation rates, while at higher recirculation rates, the time required to obtain complete pectin hydrolysis into the fluidized reactor was found to be 0.25 times smaller than in the packed bed reactor: 131 min for the packed reactors and 41 min for the fluidized reactors.

Production of low-lactose milk by means of nonisothermal bioreactors.

The effect of the immobilization time on the activity of immobilized β‐galactosidase from K. lactis was investigated. Six biocatalytic membranes, different only for the time of the enzyme immobilization, were obtained by using nylon membranes grafted with glycidyl methacrylate (GMA) and activated by hexamethylenediamine (HMDA) and glutaraldehyde (Glu), used as spacer and coupling agent, respectively. Comparison between the isothermal and nonisothermal yield of these biocatalytic membranes was carried out in the process of lactose hydrolysis in milk. All of the results, reported as a function of the immobilization time, have evidenced the influence of our variable parameter on the activity of the catalytic membranes. The membrane giving highest yield under isothermal and nonisothermal conditions was that obtained with 2 h of immobilization time. The industrial application of these membranes has been discussed in terms of percentage reduction of the production times.

Hollow‐Fiber Enzyme Reactor Operating under Nonisothermal Conditions

A hollow‐fiber enzyme reactor, operating under isothermal and nonisothermal conditions, was built employing a polypropylene hollow fiber onto which β‐galactosidase was immobilized. Hexamethylenediamine and glutaraldehyde were used as spacer and coupling agent, respectively. Glucose production was studied as a function of temperature, substrate concentration, and size of the transmembrane temperature gradient. The actual average temperature differences across the polypropylene fiber, to which reference was done to evaluate the effect of the nonisothermal conditions, were calculated by means of a mathematical approach, which made it possible to know, using computer simulation, the radial and axial temperature profiles inside the bioreactor and across the membrane. Percent activity increases, proportional to the size of the temperature gradients, were found when the enzyme activities under nonisothermal conditions were compared to those measured under comparable isothermal conditions. Percent reductions of the production times, proportional to the applied temperature gradients, were also calculated. The advantage of employing nonisothermal bioreactors in biotechnological industrial process was discussed.

Reduction of Active Elastase Concentration by Means of Immobilized Inhibitors: A Novel Therapeutic Approach

The inhibitory power of three different active Nylon membranes, separately loaded with three different protease inhibitors, was studied with the aim of reducing the increased elastase concentration occurring during hemodialysis or extracorporeal blood circulation in patients undergoing cardiopulmonary bypass. Chemical grafting was carried out to make the inert Nylon membrane suitable for the immobilization of the inhibitors. The behavior of immobilized α1‐antitrypsin, bovine pancreatic trypsin inhibitor (BPTI), or elastatinal was separately studied. α1‐Antitrypsin and BPTI were covalently immobilized by means of a diazotization process, whereas elastatinal was covalently attached via a condensation process mediated by glutaraldehyde. The inhibitory power of each membrane type was studied as a function of the amount of immobilized inhibitor and temperature. All active membranes have shown good inhibitory power. The most efficient membrane was that loaded with α1‐antitrypsin, the less efficient that with BPTI.