ABSTRACT
Climate changes are inducing increased sugar levels of must, which produces negative effects on wine quality, as unbalanced wines with high degrees of alcohol. So, effective strategies to control the increase of sugar levels in must have been studied. One of them is the use of a membrane process, and this is applied in this work. The sugar level of white must from Verdejo (Vitis vinifera variety) was reduced using diverse membrane processes, and the effect of this fact on the volatile composition of the corresponding wines is studied. The study was carried out during three consecutive vintages. An important impact of the reduction of sugar levels of must on the volatile composition of the obtained wines was detected, which was due to some retention phenomena of aromatic and precursor compounds. To minimize the volatile composition modifications, an appropriate selection of the nanofiltration membrane must be done.
Subject(s)
Carbohydrates/analysis , Volatile Organic Compounds/analysis , Wine/analysis , Amino Acids/analysis , Filtration/methods , Food Handling/methods , Fruit/chemistry , VitisABSTRACT
Silicon wafers have been silylated with VTMS (vinyltrimethoxysilane) and hydrolyzed. Subsequently, PVP (polyvinyl pyrrolidone) was grafted onto the silylated surface by two different techniques: the grafting-through (GT) and the grafting-onto techniques (GO). The measurement of contact angles along with the topography analysis by atomic force microscopy (AFM) has allowed monitoring the different stages of the process and the temporal evolution of polymer grafting. The results have demonstrated the feasibility of both methods of grafting but have shown that the GT method gives a higher density of polymer-grafted chains. The AFM technique in adequate liquid environments has been proven to permit the surface density of chains to be distinguished by both methods and to estimate the length of the resulting PVP chains.
ABSTRACT
The mass of gamma-globulin fouling an Anodisc alumina membrane with a nominal pore diameter of 0.1 µm has been measured at several concentrations and pHs. This fouling resulted from filtering through the membrane in a continuous recirculation device. The low-concentration fouling can be attributed mainly to adsorption. The complete concentration dependence of fouling mass has been obtained and fitted to a Freundlich heterogeneous isotherm, from which the pH dependence of active fouling sites and energies has been also obtained. Adsorption is studied as a function of the electrostatic forces between the solute and the membrane. A sharp maximum in the adsorbed mass for zero electrostatic force is observed. At high concentrations, accumulation plays a relevant role at alkaline pH, as confirmed by flux decay experiments, retention measurements, and AFM (atomic force microscopy) pictures. Copyright 2000 Academic Press.
ABSTRACT
The flux decline, is studied in typical experiments with dead-end microfiltration of BSA solutions (1, 3, 5 and 10 g/L) through Cyclopore track-etched polycarbonate membranes (nominal pore size 0.1 µm) at several pH values and two ionic strengths. Results have been analyzed in terms of the common blocking laws and correlated with the operation parameters. Variations of pressure, concentration, pH, and ionic strength have shown great influence on the kinetics of protein deposition. In any case, the process of membrane fouling can be divided in two steps, clearly separated in all the experiments: a rapid initial internal blocking, strongly dependent on operation parameters, and a final stage of external blocking with lower sensitivity of the flux behavior on operation conditions. Finally, the amount of adsorbed protein and its influence on pore size distribution have been analyzed by desorption with a SDS-solution and by an extended bubble point method. These results show that the initial internal pore blocking can be attributed to protein adsorption while the long-time fouling should be caused mainly by solute-solute interactions.
ABSTRACT
Flux and retention of 0.1%w/w aqueous solutions of several proteins [lysozyme, pepsin, bovine serum albumin (BSA), lipase, and gamma-globulin] with molecular weights of 14.6, 36, 67, 801 and 150 kDa are studied when they are tangentially filtered, with transmembrane pressure differences until 1 MPa and circulation velocities in the re-tentate loop from 0.04 to 1.98 m/s (laminar regime), through two asymmetric polysulfone commercial membranes (E-100 with a nominal pore size of 0.01 mum and E-500 with a nominal pore size of 0.04 mum). Results are analyzed with the film theory for the concentration-polarization phenomenon, obtaining the mass transfer coefficient along with the apparent and true retention coefficients for the cell used, as a function of the feed circulation velocity and the molecular weight of the solute. The standard retention curves lead to pore size distributions differing from the nominal ones. These differences can be attributed to the modifications of the membranes when they are in operational conditions, probably due to protein adsorption. (c) 1995 John Wiley & Sons, Inc.
