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The hydrolysis of cellulose to the water-soluble products cellobiose and glucose is achieved via synergistic action of cellulolytic proteins. The three types of enzymes involved in this process are endoglucanases, cellobiohy-drolases, and β-glucosidases. One of the best fungal cellulase producers is RUT C30. However, the amount of β-glucosidases secreted by this fungus is insufficient for effective cellulose conversion. We investigated the production of cellulases and β-glucosidases in shake-flask cultures by applying three pH-controlling strategies: ()the pH of the production medium was adjusted to 5.8 after the addition of seed culture with no additional pH adjustment performed, () the pH was adjusted to 6.0 daily, and () the pH was maintained at 6.0 by the addition of Tris-maleate buffer to the growth medium. Different carbon sources-Solka Floe 200, glucose, lactose, and sorbitol—were added to standard Mandels nutrients. The lowest β-glucosidase activities were obtained when no pH adjustment was done regardless of the carbon source employed. Somewhat higher levels of β-glucosidase were measured in the culture filtrates when daily pH adjustment was carried out. The effect of buffering the culture medium on β-glucosidase liberation was most prominent when a carbon source inducing the production of other cellulases was applied.

The objective of this work was to select an efficient methodology for preparing active samples of lipase immobilized in wood cellulignin, to be applied in hydrolysis and ester reactions. For this purpose, lipase was immobilized in the matrix by physical adsorption (pure cellulignin) and covalent binding (activated cellulignin with glutaraldeyde or carbonyldiimidazole [CDI]) in the presence or absence of polyethylene glycol (PEG) (Molecular mass of 1500 Daltons) as stabilizing agent. The activating agent and the presence of PEG-1500 in the immobilization procedure showed a strong influence on enzyme retention in the support. The values for enzyme retention ranged from 20 to 68%, and the highest yield was obtained when the enzyme was immobilized in cellulignin activated with CDI in the presence of PEG-1500. This immobilized derivative presented high hydrolytic (193.27 µ/[mg · min]) and synthetic (522.92 µ/[g · min]) activities when compared with those obtained by other techniques. The superiority of this immobilized system was confirmed by additional analyses, such as infrared spectroscopy and elemental analysis, which demonstrated an appropriate enzyme fixation and the highest level of protein incorporation in the support. Further information on the immobilized derivative was obtained by assessing the recycle potential in both aqueous and nonaqueous media.

In this article, we report the development and optimization of an industrial culture medium for the production of extracellular lipase in the yeast . Until now olive oil in combination with glucose was used as the carbon source and inducer for the production of lipase. Our results demonstrate that methyloleate, a cheap hydrophobic compound, could efficiently substitute olive oil as the inducer and carbon source for lipase production. A new process of lipase production was developed yielding a twofold increase in the level of production compared with the levels in previous reports.

Different soluble NAD-dependent alcohol dehydrogenase (ADH) isozymes were detected in cell-free homogenates from aerobically grown mycelia of YR-1 strain of isolated from petroleum-contaminated soil samples. Depending on the carbon source present in the growth media, multiple NAD-dependent ADHs were detected when hex-adecane or decane was used as the sole carbon source in the culture media. ADH activities from aerobically or anaerobically grown mycelium or yeast cells, respectively, were detected when growth medium with glucose added was the sole carbon source; the enzyme activity exhibited optimum pH for the oxidation of different alcohols (methanol, ethanol, and hexadecanol) similar to that of the corresponding aldehyde (∼7.0). Zymogram analysis conducted with partially purified fractions of extracts from aerobic mycelium or anaerobic yeast cells of the YR-1 strain grown in glucose as the sole carbon source indicated the presence of a single NAD-dependent ADH enzyme in each case, and the activity level was higher in the yeast cells. ADH enzyme from mycelium grown in different carbon sources showed high activity using ethanol as substrate, although higher activity was displayed when the cells were grown in hexadecane as the sole carbon source. Zymogram analysis with these extracts showed that this particular strain of has four different isozymes with ADH activity and, interestingly, one of them, ADH4, was identified also as phenanthrene-diol-dehydrogenase, an enzyme that possibly participates in the aromatic hydrocarbon biodegradation pathway.

Accumulation of poly hydroxyalkanoate (PHA) from excess activated sludge (EAS) was monitored and controlled via the oxidation-reduction potential (ORP) adjusting process. The ORP was adjusted and controlled by only regulating the gas-flow rate pumped into the cultural broth in which sodium acetate (C2) and propionate (C3) were used as carbon sources. Productivity of PHA and the PHA compositions at various C2 to C3 ratios were also investigated. When ORP was maintained at +30 mV, 35% (w/w) of PHA of cell dry weight obtained when C2 was used as sole carbon source. The PHA copolymer, poly-(3-hydroxybutyrate-co-3-hydroxyvaler-ate) (PHBV), accumulated by EAS with different 3-hydroxyvalarate (3HV) molar fractions ranged from 8% to 78.0% when C2 and C3 was used as sole carbon source, By using ORP to monitor and control the fermentation process instead DO meter, the ORP system provided more precise control to the PHA accumulation process from EAS under low dissolved oxygen (DO) concentrations. Adjusting the C2 to C3 ratios in the media could control the composition such as the 3HV/3HB ratios of the PHBV. Furthermore, it might be an effective way to adjust the 3HV molar fractions in PHBV by controlling the DO concentration via the ORP monitoring system. The 3HV molar fractions in the PHBV declined with increasing ORP from -30 mV to +100 mV by adjusting the gas-flow rate (i.e. the DO concentration). It is concluded that the DO plays a very important role in the synthesis of 3HV subunits in PHBV co-polymer from the EAS. Therefore, a hypothetic metabolic model for PHA synthesis from EAS was proposed to try to explain the results in this study.

Crops such as switchgrass ( L.), bermudagrass ( L.), or napiergrass ( Schumach.) have the capacity to produce large quantities of lignocellulose for biofuel (). To facilitate use of lignocellulosic material for ethanol, it will be necessary to determine cost-efficient pretreatments to enhance the conversion to fermentable sugars. The lignified residual products from ethanol production could also provide a value-added co-product for industrial feedstocks (e.g., nutritional antioxidants, ultraviolet absorbers, resins).

A isolate was shown to be able to produce extracellular protease in solid-state fermentations (SSF) using soy cake as culture medium. A significant effect of inoculum concentration and physiological age on protease production was observed. Maximum activities were obtained for inoc-ula consisting of exponentially growing cells at inoculum concentrations in the range of 0.7–2.0 mg g. A comparative study on the influence of cultivation temperature and initial medium pH on protease production in SSF and in submerged fermentation (SF) revealed that in SSF a broader pH range (5–10), but the same optimum temperature (37°C), is obtained when compared to SF. A kinetic study showed that enzyme production is associated with bacterial growth and that enzyme inactivation begins before biomass reaches a maximum level for both SF and SSF. Maximum protease activity and productivity were 960 U g and 15.4 U g h for SSF, and 12 U mL and 1.3 U mL h for SF. When SSF protease activity was expressed by volume of enzyme extract, the enzyme level was 10-fold higher and the enzyme productivity 45% higher than in SF. These results indicate that this bacterial strain shows a high biotechnological potential for protease production in solid-state fermentation.

Corn fiber is the fibrous by-product of wet-mill corn processing. It typically consists of about 20% starch, 14% cellulose, and 30% hemicellulose in the form of arabinoxylan. Crude corn fiber (CCF) was fractionated into de-starched corn fiber (DSCF), corn fiber with cellulose (CFC) enriched, and corn fiber arabinoxylan (CFAX), and these fractions were evaluated as substrates for enzyme production by QM9414 and Rut C-30 grew on CCF, DSCF, CFC, or CFAX and secreted a number of hydrolytic enzymes. The enzymes displayed synergism with commercial cellulases for corn fiber hydrolysis.

Bacteria of genus are active producers of extracellular proteases, and characteristics of enzyme production by species have been well studied. The aim of this experimental study is isolation and partial purification of protease enzyme from the bacteria species. Protease enzyme is obtained by inducing spore genesis of bacteria from species on suitable media. The partial purification was reali-zed by applying successively ammonium sulfate precipitation, dialysis, DEAE-cellulose ion exchange chromatography to the supernatant. In this study, the effect of substrate concentration, reaction time, the effect of inhibitor and activator on the optimum pH, optimum temperature, pH stability, and temperature stability was determined. Molecular weight of the obtained enzyme was investigated by SDS-PAGE. In this study, the specific activity of the supernatant, which was partially purified from bacteria, was 10.4 U/mg, specific activity of supernatant was 13.5 U/mg after 80% ammonium sulfate fractionation. The final enzyme preparation was 1.1-fold purer than the crude homogenate. Molecular weight of the protease was determined, and it was found that the weight of enzyme was 45 kDa by using SDS-PAGE.

The hydrolytic activity of fungal originated β-glucosidase is exploited in several biotechnological processes to increase the rate and extent of saccha-rification of several cellulosic materials by hydrolyzing the cellobiose which inhibits cellulases. In a previous presentation, we reported the screening and liquid fermentation with , strain for p-glucosidase production at shake flask cultures in a basal culture medium with mineral salts, corn syrup liquor, and different waste lignocellulosic materials as the sole carbon source obtaining the maximum enzymatic activity after 5–6 d of 8.5 IU/mL using native sugar cane bagasse. In this work we describe the evaluation of fermentation conditions: growth temperature, medium composition, and pH, also the agitation and aeration effects for β-glucosidase production under submerged culture using a culture media with corn syrup liquor (CSL) and native sugar cane bagasse pith as the sole carbon source in a laboratory fermenter. The maximum enzyme titer of 7.2 IU/mL was obtained within 3 d of fermentation. This indicates that β-glucosidase productivity by is function of culture conditions, principally temperature, pH, culture medium conditions, and the oxygen supply given in the bioreactor. Results obtained suggest that this strain is a potential microorganism that can reach a major level of enzyme production and also for enzyme characterization.