Biomedical subjects

F Maugeri

Publications and source records attributed to F Maugeri.

4 recordsLinked to original sources

PubMed2001

Studies on lipase-affinity adsorption using response-surface analysis.

Lipases are widely distributed enzymes that can be obtained from animals, plants and micro-organisms. Coupling lipases with a wide range of substrates allows the opportunity for synthesis of optically pure pharmaceutical preparations, flavour compounds and other food additives. Affinity chromatography owes its power as a purification method to specific biological interactions. Response-surface analysis was chosen to study column efficiency. This method allows the understanding of interactions between variables with advantages over conventional methods, which involve changing one variable while fixing others at certain levels. The aim of this work was to study the influence of the ratio bed height/column diameter (L/D) and superficial velocity (V) on the column efficiency. The experimental design involved the two variables, L/D (2-10) and v (1-2 cm/min), at five levels. Lipase was obtained from Geotrichum sp. culture in a complex medium composed of 5% corn-steep liquor, 0.5% NH(4)NO(3) and 1% olive oil at 30 degrees C, with 1VVM (air volume/medium volume per min) aeration and 400 rev./min agitation. Maximum lipase activity was 19 units/ml after almost 9 h of fermentation. This lipase could potentially be used in esterification reactions to increase the content of gamma-linolenic acid and to produce bioaromas for food industries. The adsorption assays were carried out in a fixed-bed column with an affinity adsorbent, which was obtained by reaction of a gel with oleic acid as ligand. Breakthrough curves were obtained for all experiments. It has been shown that the lower the values of both L/D and v, the higher the column efficiency (maximum 65.43%). Also, it was observed from the response surface that the efficiency reached a minimum at an L/D of around 8.

Adsorption↗

PubMed2001

Kinetics of ethanol fermentation with high biomass concentration considering the effect of temperature.

A model of ethanol fermentation considering the effect of temperature was developed and validated. Experiments were performed in a temperature range from 28 to 40 degrees C in continuous mode with total cell recycling using a tangential microfiltration system. The developed model considered substrate, product and biomass inhibition, as well as an active cell phase (viable) and an inactive (dead) phase. The kinetic parameters were described as functions of temperature.

Biomass↗

PubMed2001

Optimization of inulinase production by Kluyveromyces marxianus using factorial design.

Factorial design and response surface techniques were used to optimize the culture medium for the production of inulinase by Kluyveromyces marxianus. Sucrose was used as the carbon source instead of inulin. Initially, a fractional factorial design (2(5-1)) was used in order to determine the most relevant variables for enzyme production. Five parameters were studied (sucrose, peptone, yeast extract, pH, and K2HPO4), and all were shown to be significant. Sucrose concentration and pH had negative effects on inulinase production, whereas peptone, yeast extract, and K2HPO4 had positive ones. The pH was shown to be the most significant variable and should be preferentially maintained at 3.5. According to the results from the first factorial design, sucrose, peptone, and yeast extract concentrations were selected to be utilized in a full factorial design. The optimum conditions for a higher enzymatic activity were then determined: 14 g/L of sucrose, 10 g/L of yeast extract, 20 g/L of peptone, 1 g/L of K2HPO4. The enzymatic activity in the culture conditions was 127 U/mL, about six times higher than before the optimization.

Analysis of Variance↗

PubMed2000

Simulated dynamics and control of an extractive alcoholic fermentation.

In this study, we investigated the dynamics of a computer simulation of a continuous alcoholic fermentation process combined with a flash column under vacuum. The alcohol was partially extracted in order to maintain its concentration at about 40 kg/m3 in the fermentor. The mathematical model of the fermentation was developed for industrial conditions and considers the effect of the temperature on the kinetic parameters. The performance of the dynamic matrix control algorithm, single input single output and multiple input multiple output, for the control of the extractive process was studied. The concepts of factorial design were used in a simulation study to determine the best control structures for the process.

Biomass↗