Braz. J. Chem. Eng. vol.22 número4

when using the wavelet transform analysis Toolbox.. Figure 3: Treatment of the images of the bacterium Str. clavuligerus: a) Grey-scale image; b) Binary image after thresholding;

Solutions provided by the mathematical model structure, i.e., the set of functions that describe the specific rates of microbial growth, glucose uptake and polysaccharide

Based on this hypothesis, part of the biomass was transferred from the denitrifying reactor to a second reactor, which was operated under optimal conditions to study the

In a study of anaerobic digestion of long-chain fatty acids in UASB reactors, Rinzema and Lettinga (1993), observed that concentrations of lipid in the influent equal to or higher

The specific level of substrate conversion into methane in the reactors appeared to be unaffected by addition of PCP up to concentrations of 6.0 mg.l -1 in the reactor

Figure 5: SP Sepharose Fast Flow ion-exchange chromatographic profiles for the separation of recombinant aprotinin from CTI. Feed: eluted fractions from the

The kinetics of dissolution of processed lysozyme at pH 3.5 and pH 4.5 (Figure 8) as well as X-ray diffraction analysis (Figure 9) of original and processed samples of lysozyme

data, it was possible to determine and quantify that some of the Fe species function as charge- compensating species of the zeolite structure, with samples prepared in the solid