Synchrotron FTIR microspectroscopy of the yeast Saccharomyces cerevisiae after exposure to plasma-deposited nanosilver-containing coating.

The present work was focused on elucidating changes in the model yeast Saccharomyces cerevisiae (cell composition, ultrastructure) after exposure to antimicrobial plasma-mediated nanocomposite films. In order to achieve this, a nanosilver-containing coating was deposited onto stainless steel using radiofrequency HMDSO plasma deposition, combined with simultaneous silver sputtering. X-ray photoelectron spectroscopy (XPS) confirmed the presence of silver nanoparticles embedded in an organosilicon matrix. In addition, scanning electron microscopy (SEM) demonstrated the nanoparticle-based morphology of the deposited layer. The antifungal properties towards S. cerevisiae were established, since a 1.4 log reduction in viable counts was observed after a 24-h adhesion compared to control conditions with the matrix alone. Differences in cell composition after exposure to the nanosilver was assessed for the protein region using, for the first time, synchrotron Fourier-transform infrared (FTIR) microspectroscopy of single S. cerevisiae cells, through in situ mapping with sub-cellular spatial resolution. IR spectrum of yeast cells recovered after a 24-h adhesion to the nanosilver-containing coating revealed a significant downshift (20 cm(-1)) of the amide I peak at 1655 cm(-1), compared to freshly harvested cells. This lower band position, corresponding to a loss in alpha-helix structures, is indicative of the disordered secondary structures of proteins, due to the transition between active and inactive conformations under nanosilver-induced stress conditions. No significant effect on the nucleic acid region was detected. The inhibitory action of silver was targeted against both cell wall and intracellular proteins such as enzymes. Transmission electron microscopy (TEM) observations of the yeast ultrastructure confirmed serious morphological and structural damages. A homogeneous protein-binding distribution of nanosilver all over the cell was assumed, since the presence of electron-dense silver clusters was detected not only on the cell surface but also within the cell. For control experiments with the organosilicon matrix alone, no antimicrobial effect was observed, which was consistent with synchrotron FTIR results and TEM observations.

Feasibility study of a compact process for biological treatment of highly soluble VOCs polluted gaseous effluent.

Volatile organic compounds (VOCs), representing a wide range of products mainly generated by industrial activity, are involved in air pollution. This study deals with a new biological treatment process of gaseous effluent combining a gas/liquid contactor called an "aero-ejector" and a membrane bioreactor. Combining these two innovative technologies enables a high elimination efficiency to be reached. We first focus on transfer phenomena characterization in a pilot installation on a laboratory scale, using a gaseous effluent polluted with a low ethanol concentration (7.1 x 10(-3) kg.m(-3)). These experiments demonstrated the good transfer performances since 90% of the ethanol was absorbed in the liquid phase in one step. After this physical characterization, the biological aspect of the system was studied using the yeast Candida utilis as microorganism. During the experiment, no ethanol was measured in the fermentation broth nor in the outlet gas, confirming the efficiency of ethanol elimination by C. utilis. The experimental procedure emerging from the present study strongly validates the suitability of this process for ethanol removal from air.

Influence of a transverse flowrate on the oxygen transfer performance in heterogeneous aeration: case of hydro-ejectors.

This paper deals with the scaling of aeration devices, and more specifically hydro-ejectors, in the case of heterogeneous aeration. Because the transfer of oxygen only occurs in a very small part of the volume of the treatment basin, the transfer performance of the aerator depends on the device itself and on the surrounding flow characteristics. First experiments were achieved with a 10 L mechanically agitated reactor in order to operate at a known kLa and liquid flowrate Q. The results show that the oxygen transfer capacity of the reactor is used to a greater or lesser extent depending on the flowrate which passes through the bubbling region. When a hydro-ejector is concerned, the oxygen transfer occurs inside an aerated zone of about 2 m3; experiments carried out with an industrially scaled HE in a 120 m3 test basin allowed to estimate that the kLa in this zone is about 700-800 h(-1). Applying a compartment model, it is then possible to determine the oxygen transfer capacity of the HE as a function of the transverse liquid flowrate. While this OC is 3 kg O2/h under the test basin conditions, it reaches up to 12 kg O2/h under industrial flow conditions. This value was obtained in the aerobic biological treatment of the washing waters of a sugar refinery where two 33,000 m3 basins aerated by 152 HE could degrade 35 t/d of COD.

Yeast suspension filtration: flux enhancement using an upward gas/liquid slug flow-application to continuous alcoholic fermentation with cell recycle.

This study deals with the use of an upward gas/liquid slug flow to reduce tubular mineral membrane fouling. The injection of air into the feedstream is designed to create hydrodynamic conditions that destabilize the cake layer over the membrane surface inside the filtration module complex. Experimental study was carried out by filtering a biological suspension (yeast) through different tubular mineral membranes. The effects of operating parameters, including the nature of the membrane, liquid and gas flowrates, and transmembrane pressure, were examined. When external fouling was the main limiting phenomenon, flux enhancements of a factor of three could be achieved with gas sparging compared with single liquid phase crossflow filtration. The economic benefits of this unsteady technique have also been examined. To investigate the possibility of long-term operation of the two-phase flow principle, dense cell perfusion cultures of Saccharomyces cerevisiae were carried out in a fermentor coupled with an ultrafiltration module. The air injection allowed a high and stable flux to be maintained over 100 h of fermentation, with a final cell concentration of 150 g dry weight/L. At equal biomass level, a twofold gain in flux could be attained compared with classical steady crossflow filtration at half the cost.