Abstract (1) Background: Oxygen supply is an important parameter to be considered in submerged cultures. This study evaluated the influence of different conditions for dissolved oxygen (DO) concentration on laccases activities and growth of Pleurotus sajor-caju PS-2001 in submerged process in stirred-tank bioreactor. (2) Methods: Initially, three different conditions were tested: uncontrolled DO and minimum levels of 30% and 80% of saturation, with the pH controlled between 4.5 and 7.0. (3) Results: Best results were observed at 30% DO (26 U mL-1 of laccases at 96 h), whereas higher mycelial biomass was observed at 30% and 80% DO (above 4.5 g L-1). Four different conditions of DO (uncontrolled, 10%, 30% and 50% of saturation) were tested at pH 6.5, with higher laccases activity (80 U mL-1 at 66 h) and lower mycelial growth (1.36 g L-1 at 90 h) being achieved with DO of 30%. In this test, the highest values for volumetric productivity and specific yield factor were determined. Under the different pH conditions tested, the production of laccases is favoured at DO concentration of 30% of saturation, while superior DO levels favours fungal growth. (4) Conclusion: The results indicate that dissolved oxygen concentration is a critical factor for the culture of P. sajor-caju PS-2001 and has important effects not only on laccases production but also on fungal growth.

(1) Background: In this study, the effects of different pH values (2.4, 3.2, 4.4 and 5.0), temperatures (30, 35, 40, 45 and 50°C) and agitation (100 rpm) on the enzymatic decolourisation of twenty-two dyes belonging to the chromophore groups anthraquinone, azo and triphenylmethane were assessed. (2) Methods: In all conditions, it was used a crude enzyme broth containing 30 U mL-1 laccases produced by Pleurotus sajor-caju PS-2001 in submerged process. (3) Results: Regarding the effects of pH values, the best results were obtained at pH 3.2 and 30°C, in which bleaching was observed for all dyes evaluated. In assays conducted at different temperatures, highest levels of decolourisation were observed at 35°C and pH 3.2 for nineteen of the dyes assessed. Thirteen dyes presented colour reduction exceeding 50% after the enzymatic treatment, including all acid and all disperse dyes evaluated. The reciprocal agitation of 100 rpm promoted negative effect on decolourisation. (4) Conclusion: From the results achieved, one can conclude that the laccase-containing preparation of P. sajor-caju PS-2001 has potential for the decolourisation of some dyes widely used in different industrial sectors, especially in the textile industry, and therefore could be used in future strategies for the biotreatment of coloured wastes.

In this work, a protocol for the formulation of an enzyme concentrated product to be applied in fruit juice treatment is described. Downstream processing conditions for the recovery and concentration of pectinases produced by the new strain Aspergillus niger LB-02-SF in solid state cultivation were assessed. The solid-liquid ratio in the extraction step of pectinases recovery from the cultivated media was evaluated and the highest activity was obtained with a solid-liquid ratio of 1:10. The crude extract was concentrated by ultrafiltration and the total pectinase (TP) activity was 73.6-fold concentrated in relation to the crude extract, and a final TP titer of 663 U mL–1 was obtained with 73.7% of recovery yield. KCl and different glycerol concentrations were added to the concentrated extract and the stability of pectinases during the storage at 5°C for 59 weeks was tested. The formulation with 50% w/w glycerol was applied to the treatment of apple and grape juices and the results of these tests were statistically comparable to those obtained with two high-quality commercial preparations.

In the present study, the effect of pectinases on the production of pulp and juice of araçá and the presence of bioactive compounds were evaluated. An enzyme extract (EE) produced by Aspergillus niger LB-02-SF in solid state fermentation and the commercial enzyme Ultrazym®AFP-L were used in this study. After enzyme treatment with the EE preparation, the extraction yield increased by 23.1% and viscosity decreased by 42.8%, during pulp maceration. During juice processing, there was an increase of 70.6% in clarification and a decrease of 72.87% in turbidity. Higher values of these parameters, 47.7, 69.0, 80.7, and 79.7%, respectively, were obtained using the Ultrazym®AFP-L, which also led to a significant increase in the polyphenol content, both in the pulp (24%) and in the juice (28%), with a less pronounced effect when the EE was applied (10 and 21%, respectively). The anthocyanins content in the araçá pulp increased after treatment with the commercial preparation (23%), and there was no significant increase with the use of EE. The use of Ultrazym®AFP-L increased the β-carotene content by 29.4% in the fruit pulp, while the treatment with EE did not result in significant changes compared with those of the juice and pulp controls.

Endo-polygalacturonase (endo-PG) production by Aspergillus niger T0005/007-2 in solid medium with 170 mm of height was evaluated in a cylindrical double surface bioreactor in 96-h experiments. Cell concentration close to 92 mg.g -¹ dm (mg per g of dry medium) in the standard condition (static) was achieved, whereas in tests under forced aeration of 1.4 and 2.8 L.min-1. Kg-1 mm (L of air per minute per Kg of moist medium) and with the central shaft fungal biomass attained approximately 100 mg.g-1 dm. Superior endo-PG activity was obtained with the central-shaft system, 78 U.g-1 dm (units per g of dry medium). Forced aeration and pressure pulse showed no positive effect on the production of endo-PG, 45 U.g-1 dm and 28 U.g-1 dm, respectively. None of the conditions evaluated was efficient for medium temperature control. Endo-PG was stable up to 40ºC. The activity decreased in 50% after 120 minutes at 50ºC, which is a temperature normally found during this process.

Um meio líquido contendo farelo de trigo, sais e fonte de indutor (pectina) foi definido para a produção de exo e endo-poligalacturonases por Aspergillus oryzae CCT3940. A indução por pectina purificada foi significativamente maior que a observada com cascas de cítricos. O crescimento de A. oryzae é favorecido por valores de pH próximos a 4, embora uma queda até valor em torno de 3 seja necessária para a produção das enzimas. Posteriormente, atividades decrescentes foram observadas com a subida normal do pH até próximo à neutralidade. As maiores atividades foram alcançadas quando o processo foi iniciado em pH 4 e controlado quando decresceu até níveis ligeiramente abaixo de 3 (159 unidades.mL-1 para endo-PG, em 83 h, e 45 unidades.mL-1, em 64 h, para exo-PG), com a perda de atividades sendo drasticamente reduzida. Os melhores valores de pH e temperatura para a ação de exo-PG (4,5/57°C) e endo-PG (4,3/40ºC) foram estimados.

A liquid medium containing wheat bran, salts and a source of inducer (pectin) was found to be suitable for the production of exo- and endo-polygalacturonases by Aspergillus oryzae CCT3940. Induction of polygalacturonases by purified pectin was significantly higher than when rinds of citrus fruits were used as inducer. A. oryzae growth was favoured by pH close to 4, although a drop of pH to around 3 was needed for enzymes production. Afterwards, decreasing activities were observed with the normal increase in pH to near neutrality. The highest activities were achieved with an initial pH of 4 and controlled when it decreased to a value slightly below 3 (159 units endo-PG.mL-1 at 83 h and 45 units exo-PG.mL-1 at 64 h), being the loss in polygalacturonases activities strongly reduced at this condition. The best values of pH and temperature for the action of exo-PG (4.5/57ºC) and endo-PG (4.3/40ºC) were assessed.

Sorbitol e ácido glucônico são produzidos por células previamente cultivadas da bactéria produtora de etanol Zymomonas mobilis pela ação das enzimas periplasmáticas glicose-frutose oxidorredutase (GFOR) e glucono-delta-lactonase (GL). A atividade de GFOR/GL em células a serem empregadas nesta bioconversão depende das condições de crescimento. Em cultivo em regime descontínuo, com concentrações iniciais de glicose (S0) entre 42 e 230 g/L, as maiores atividades específica e total de GFOR/GL foram obtidas com S0 = 153 g/L (12,6 U/g de células e 62 U/L), enquanto maiores S0 levaram a atividades decrescentes em células não tratadas. Com S0 = 209 g/L, a atividade específica final foi de 7 U/g, mas, após a ruptura das células, atividade superior a 15 U/g foi medida. Uma vez que em descontínuo observou-se inibição por substrato com S0 a partir de 153 g/L, ensaios em regime descontínuo alimentado, com glicose equivalente a 230 g/L em descontínuo, foram realizados. Embora a inibição pelo substrato tenha sido superada, a atividade permaneceu baixa (5,2 U/g). Um novo ensaio em descontínuo alimentado, conduzido sob baixa pressão para remover o etanol do meio, resultou em atividade específica de 9,8 U/g e total de 68,7 U/L. Estes resultados indicam que as baixas atividades em células de Z. mobilis cultivadas com maiores S0 se deveram a mudanças na parede celular, provocadas por concentrações elevadas de etanol, que dificultaram o transporte de substrato para as enzimas intracelulares durante a bioconversão. Esta conclusão foi confirmada em ensaios de bioconversão com células provenientes de cultivos em diferentes condições.

Previously grown cells of the ethanologenic bacterium Zymomonas mobilis produce sorbitol and gluconic acid, in reactions catalysed by the periplasmic enzymes glucose-fructose oxidoreductase (GFOR) and glucono-delta-lactonase (GL). The GFOR/GL system activity, in cells to be used in this bioconversion, depends on growth conditions. In batch runs, with initial glucose concentrations (S0) from 42 to 230 g/L, the highest specific and total GFOR/GL activities were obtained with S0 = 153 g/L (12.6 U/g cells and 62 U/L). Higher S0 led to decreasing activities in fresh cells. With S0 = 209 g/L, the final specific activity was only 7.0 U/g. After disruption of cells, however, an activity over 15 U/g was revealed. Since growth inhibition with S0 over 153 g/L was observed in batch mode, fed-batch runs, equivalent to a batch of 230 g/L, were done. Although no growth inhibition occurred in fed-batch cultivation, enzyme activity remained low (5.2 U/g). A further fed-batch experiment, carried out under low pressure to remove ethanol from the medium, resulted in a specific activity of 9.8 U/g and a total activity of 68.7 U/L. These results indicate that the low GFOR/GL activities in Z. mobilis cells grown on higher S0 were due to changes in the cell wall, caused by high concentration of ethanol, that hindered the transport of the substrate to the intracellular enzymes in biconversion runs. This conclusion was confirmed by bioconversion runs with cells cultivated under different conditions.