Influence of Oxygen Supply on Growth and Laccases Production by Pleurotus sajor-caju PS-2001 in Submerged Process

(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 of laccases at 96 h), whereas higher mycelial biomass was observed at 30% and 80% DO (above 4.5 g L). 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 at 66 h) and lower mycelial growth (1.36 g L 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.


INTRODUCTION
The genus Pleurotus is a cosmopolitan group of mushrooms of high nutritional value, with therapeutic and medicinal properties. Besides their gastronomical value, these mushrooms produce molecules with HIGHLIGHTS  Dissolved oxygen (DO) concentration affects fungal growth and laccases activity.
 Synthesis of laccases is favoured when DO is controlled at 30% of saturation.
 Medium pH at 6.5, with DO at 30%, reduces growth but increases enzymatic activity.
 Under these best conditions, laccases activity of 80 U mL -1 is attained after 66 h. for 15 minutes prior to inoculation [27]. To start inoculum cultivation, three mycelial disks (1.5 cm diameter), each scraped from Petri dishes containing the fungal strain grown on maintenance medium, were added to 500-mL Erlenmeyer flasks containing 100 mL of medium. Growth occurred for 6 days under reciprocal agitation of 180 rpm at 28±2 o C. For each treatment, 10% (v/v) of inoculum were used [28].
Experiments in the bioreactor were performed in a B. Braun Biotech device model Biostat ® B in batch mode. The initial impeller speed was 200 rpm and the air flow rate was 2 L min -1 [28]. Under these conditions, the volumetric oxygen transfer coefficient (KLa) before inoculation was 12 h -1 , calculated according to the method described by Sobotka and coauthors [34] in cell-free medium. Following inoculation, dissolved oxygen (DO) concentration in the medium was at 100% of saturation, with decreasing values being observed during the process due to the metabolic activity of the microorganism.
In tests conducted under automatically controlled pH in the range between 4.5 and 7.0, three culture conditions were assessed in relation to oxygen supply. In the first condition, air flow rate and impeller speed did not change during the process and, therefore, DO content in relation to saturation decreased to 0% of saturation (uncontrolled), whereas DO concentrations in the remaining two conditions were maintained between 30 and 80% of saturation by automatic air flow rate variation.
In tests conducted at fixed pH of 6.5 [14], four cultivation conditions were evaluated with respect to the oxygen supply: uncontrolled DO and maintenance at minimum levels of 10, 30 and 50% of saturation.
In all tests, the pH was automatically controlled by adding 2 mol L -1 NH4OH or 2 mol L -1 H2SO4. Silicone antifoam agent was added to the medium before inoculation, at a ratio of 0.1 mL L -1 , as defined by Bettin and coauthors [27]. The cultivation medium volume in the bioreactor was 4 L [28]. The system was kept at a controlled temperature of 28±1 o C, and the studied variables were monitored for 168 h in the tests with pH between 4.5 and 7.0, and for 90 h when the pH was controlled at 6.5.

Sampling procedure and determination of fungal biomass
For each experiment, samples were collected, centrifuged at 3000 g for 15 minutes at 25 o C, and the supernatant was used in the analytical procedures. All determinations were done in triplicate.
Mycelial biomass was determined gravimetrically after drying at 90 o C for 24 h [28].
Manganese peroxidase (MnP) activity was assayed at 30°C using 50 g mL -1 phenol red (Merck  ) as substrate, 50 µmol L -1 MnSO4.H2O, 50 µmol L -1 H2O2, 12.5 mmol L -1 sodium lactate, 500 g mL -1 bovine albumin, 20 mmol L -1 sodium succinate buffer (pH 4.5), and 0.5 mL of culture supernatant. The reaction was stopped by adding 40 L of 2 mol L -1 NaOH to the mixture. The oxidation of phenol red was determined by measuring the increase in absorbance at 610 nm (610 = 4.46 x 10 4 mol -1 cm -1 ) [37]. For Lac and MnP, one unit of enzyme activity was defined as the amount that catalyzes the production of 1 mol of colored product per mL of sample per min.
Proteases were determined using azocasein as substrate in 50 mmol L -1 sodium phosphate buffer (pH 7.0). Reactions were conducted at 40 o C for 40 min and were stopped by adding 10% (m/v) trichloroacetic acid (TCA). Samples then rested for 15 min for complete precipitation of bigger fragments of azocasein, centrifuged at 10000 rpm for 5 min, and then 1 mol L -1 sodium hydroxide was added. Absorbance was measured spectrophotometrically at 440 nm, according to Sarath and coauthors [40]. One enzymatic unit was defined as the amount of enzyme required for producing in a 1-cm cuvette a variation in absorbance of one unit.

Determination of substrate and soluble proteins concentrations
Substrate concentration was quantified by the DNS (3,5-dinitrosalicilic acid -Sigma ® ) method proposed by Miller [41] using glucose as standard. Protein concentrations were determined by the method of Bradford [42] using bovine serum albumin as standard.

Measurement of dissolved oxygen concentration
Dissolved oxygen concentration (DO) was measured using a sterilizable polarographic electrode coupled to the bioreactor. The electrode was calibrated previously to inoculation by bubbling air and nitrogen in the cultivation medium in order to set respectively the values for 100 and 0% of the saturation in oxygen in the liquid phase.

Yield factors, productivities and specific activity
Laccases activity yield from glucose (YE/S), in U g -1 , was calculated by the relationship YE/S = [(Ef -Ei) . 1000] / (Si -Sf), where Ef is the final enzymatic activity in U mL -1 , Ei is the initial enzymatic activity in U mL -1 , Si is the initial substrate concentration in g L -1 , and Sf is the final substrate concentration in g L -1 .
Biomass yield from glucose (YX/S), in g g -1 , was calculated by the relationship YX/S = (Xf -Xi) / (Si -Sf), where Xf is the final biomass concentration in g L -1 , Xi is the initial biomass concentration in g L -1 , Si is the initial substrate concentration in g L -1 , and Sf is the final substrate concentration in g L -1 .
Specific yield factor (YE/X), in U.g-1, was calculated by the relationship YE/X = (Emax) / (Xmax), where Emax represents the maximum laccases activity in U mL -1 and Xmax the maximum biomass concentration in g L -1 .
Enzymatic productivity (PE), in U mL -1 h -1 , was calculated by the relationship PE = (Ef -Ei) / t, where Ef is the final enzymatic activity in U mL -1 , Ei is the initial enzymatic activity in U mL -1 , and t is the time of cultivation in hours.
Biomass productivity (PX ), in g L -1 h -1 , was calculated by the relationship PX = (Xf -Xi) / t, where Xf is the final cellular concentration in g L -1 , Xi is the initial cellular concentration in g L -1 , and t is the time of cultivation in hours.

Bioreactor cultivations at pH controlled between 4.5 and 7.0
During the experiments, three different conditions of oxygen concentration (DO) were tested (uncontrolled, 30% and 80% of saturation in the medium), using basic medium constituted of glucose, pure casein and mineral solution added of CuSO4 and benzoic acid as enzymatic inducers at pH controlled between 4.5 and 7.0 [28,29]. Figure 1 shows laccases activities, substrate and biomass concentrations during the 168 hours of the experiment. Amongst the conditions tested, optimal results were obtained using a 30% DO concentration in culture medium, with higher laccases activity of approximately 26 U mL -1 at 96 h of cultivation ( Figure 1B). The condition of uncontrolled DO saturation showed intermediate levels of laccases activity, with maximum titles of 18 U mL -1 also at 96 h of cultivation ( Figure 1A). However, the experiment performed at 80% saturation showed lower enzymatic titles than the other experiments s, with higher laccases activity of 7 U mL -1 at 24 h, and subsequent decrease until the end of cultivation ( Figure 1C), indicating that this high DO concentration does not favour enzyme production.
With respect to the substrate and biomass concentration data, in all conditions assayed, only residual levels of glucose were observed at 72 h of cultivation ( Figure 1), evidencing that variations in oxygen concentration did not interfere in substrate consumption. At the beginning of cultivation, fungal biomass data ( Figure 1) showed similar kinetics in all conditions assayed; however, maximum biomass during the uncontrolled condition (approximately 2.5 g L -1 at 72 h of cultivation) was lower than values obtained in the other experiments ( Figure 1A), which might be due to inadequate oxygen supply during the growth and substrate consumption phase. At 30 and 80% O2 concentrations ( Figure 1B and 1C), biomass valuesboth higher than 4.5 g L -1were reached at 72 and 90 h of cultivation, respectively.
Substrate consumption, completed at 72 h, was similar in the various conditions assayed, which might have contributed to a possible biomass lysis after 96 h of cultivation ( Figure 1), whereas there was a decrease in the biomass levels after detecting the maxima. During the experiment at 80% of saturation, the variation of the air flow rate up to a maximum of 10 L min -1 was not enough to keep DO concentration at the desired level. In fact, DO decreased sharply at 48 h of cultivation to approximately 50%. It is important to remark that the option of controlling oxygen concentration by increasing impellers speed was not used in order to avoid mycelial shearing. During the 30% experiment, concentration decreased naturally to the specified level and remained unchanged until the end of the experiment (data not shown). During the uncontrolled-DO experiment, null concentrations were detected only between 48 and 72 h, because initial culture conditions (200 rpm, 0.5 vvm) were not altered. At the end of the experiment (after 120 h), levels were restored to approximately 100%. The pH values, which were maintained between 4.5 and 7.0, were measured along the experiment and it was observed that the lowest pH that occurred after 24 h of process coincided with the lowest DO. During the cultivation, this phase showed the more intense metabolic activity; after that (from 72 h onwards), data from all conditions assayed showed a pH increase within the controlled levels (data not shown). The maximum activities of phenol-oxidases and proteases quantified in the cultures are presented in Table 1. Total peroxidases were detected in all experiments, with highest levels at 30% DO, as observed for laccases ( Figure 1B); at 80% saturation, titles were lower than 1 U mL -1 , with intermediate levels being attained with uncontrolled DO concentrations. For MnP, highest titles were obtained at 80% DO concentration. LiP and VAO activities were less than 1 U mL -1 in all conditions tested. For proteases, the highest activities (7 -10 U mL -1 ) were detected at 80% concentration right from the beginning of cultivation on, which might be related to the lower laccases activity observed during this experiment (Figure 1), together with greater mycelial damage due to high specific air flow (10 L min -1 ); in the other experiments, proteolytic activity was similar in all times evaluated, showing a small increase at the end of cultivations (maximum of 3 U mL -1 ). Lacmax (maximum laccases activity), tLac,max (time to reach the maximum laccases activity), Permax (maximum total peroxidase activity), tPer,max (time to reach the maximum total peroxidase activity), MnPmax (maximum manganese peroxidase activity), tMnP,max (time to reach the maximum manganese peroxidase activity), LiPmax (maximum lignin peroxidase activity), tLiP,max (time to reach the maximum lignin peroxidase activity), VAOmax (maximum veratryl alcohol oxidase activity), tVAO,max (time to reach the maximum veratryl alcohol oxidase activity), Proteases (maximum proteolytic activity), tProt,max (time to reach maximum protease activity), ND (enzymatic activity not detected).
For all conditions assayed, total soluble protein concentrations (TSP) were similar at the beginning of the experiments, showing an increase after 96 h and until the end of cultivations. This might be related to biomass autolysis after total substrate consumption, resulting in release of structural and intracellular proteins. It is important to emphasize that the behaviour of total protein kinetics for the 30% and 80% experiments was similar (> 130 mg L -1 after 96 h), while only the uncontrolled experiment showed lower levels (< 70 mg L -1 ) during incubation.
Overall data obtained during the experiments are shown in Table 2. Except for X,m data, all results referring to the enzyme (YE/S, PE, TSP and SALacwith relation to soluble protein and biomass concentrations) refer to the time at which maximum laccases activity was detected, while data referring to biomass (YX/S and PX) refer to the time during which maximum biomass concentration was observed. YE/X establishes the relationship between the maximum laccases activity and maximum biomass concentration, regardless of the time of cultivation.
Generally, results for all parameters referring to laccases activities (YE/S, PE, TSP and SALac) were higher in the experiment at 30% DO concentration, during which highest enzymatic activities were detected ( Figure  1B). Intermediate and lowest levels were observed in uncontrolled and 80% experiments, respectively. However, the analysis of parameters related to biomass (X,m, YX/S and PX) show that the best results were obtained for the 30% and 80% DO experiments, which were also more favourable to microorganism growth ( Figure 1B and 1C), while the uncontrolled experiment presented lower levels for all parameters evaluated. Lacmax (maximum laccases activity), tLac (time to reach maximum laccases activity), YE/S (laccases activity yield from glucose), PE (laccases volumetric productivity), TSP (total soluble proteins concentration), SALac (laccases specific activityrelated to protein and biomass concentrations), X,m (maximum specific growth rate), Xmax (maximum biomass concentration), tXmax (time to reach the maximum biomass concentration), YX/S (biomass yield from glucose), PX (biomass volumetric productivity), YE/X (specific yield factor).

Bioreactor cultivations at fixed pH of 6.5
For the strain evaluated in this work, studies conducted earlier showed an increase in the synthesis of laccases with the medium pH controlled at 6.5 (data not shown). Thus, new tests were performed using this pH value, evaluating the oxygen supply under the conditions in which the best results were observed for pH between 4.5 and 7.0: uncontrolled DO concentration and DO controlled in minimum levels of 10, 30 and 50%.
In Figure 2, the time courses for laccases activities and substrate and biomass concentrations under different conditions tested for oxygen supply are presented. As shown, DO concentrations close to 30% of saturation provide higher enzyme levels in comparison to thus determined in tests carried out with uncontrolled DO and with minimum levels of 10 and 50%, showing peak of 80 U mL -1 in 66 h of cultivation ( Figure 2C). It was observed a gradual decline in the concentration of glucose in all conditions evaluated, with concomitant increased mycelial biomass. Superior concentrations of biomass were measured at 50% DO saturation condition, with a peak of 2.8 g L -1 in 66 h of cultivation ( Figure 2D). The highest laccases production test was the one who showed the smallest fungal growth ( Figure 2C). Under uncontrolled DO and with 10% of saturation (Figure 2A and 2D), the kinetic behaviours of both substrate consumption and biomass formation were very similar.
In all experiments, the minimum levels established for DO -10, 30 and 50%have been achieved between 24 and 60 h of cultivation (data not shown). In the test carried out with uncontrolled DO, very low levels of oxygen were detected as early as 48 h, remaining at values near to 0% from 60 h until the end of the test, as a result of the fungal metabolism.
In Table 3, the maximum enzymatic activities attained and their respective maximum detection times are presented. Increased levels of laccases and total peroxidase were observed in tests with 30% DO saturation. For MnP, higher activities occurred with 50% of saturation in OD. LiP was not detected and VAO were measured only in test with 30% of DO. The proteolytic activity was less than 2 U mL -1 in all tests.  Lacmax (maximum laccases activity), tLac,max (time to reach the maximum laccases activity), Permax (maximum total peroxidase activity), tPer,max (time to reach the maximum total peroxidase activity), MnPmax (maximum manganese peroxidase activity), tMnP,max (time to reach the maximum manganese peroxidase activity), LiPmax (maximum lignin peroxidase activity), tLiP,max (time to reach the maximum lignin peroxidase activity), VAOmax (maximum veratryl alcohol oxidase activity), tVAO,max (time to reach the maximum veratryl alcohol oxidase activity), Proteases (maximum proteolytic activity), tProt,max (time to reach maximum protease activity), ND (enzymatic activity not detected).
Total soluble protein (TSP) showed maximum levels close to 500 mg L -1 in test performed with uncontrolled dissolved O2. However, in the other conditions evaluated, the values were lower than 350 mg L -1 , showing similar behaviour profiles during the process.
In Table 4, the general results obtained in cultures performed at pH 6.5 are shown. Except for X,m data, all results referring to the enzyme (YE/S, PE, TSP and SALacwith relation to soluble protein and biomass concentrations) refer to the time at which maximum laccases activity was detected, while data referring to biomass (YX/S and PX) refer to the time during which maximum biomass concentration was observed. YE/X is the relationship between the maximum laccases activity and maximum biomass concentration. Lacmax (maximum laccases activity), tLac (time to reach maximum laccases activity), YE/S (laccases activity yield from glucose), PE (laccases volumetric productivity), TSP (total soluble proteins concentration), SALac (laccases specific activityrelated to protein and biomass concentrations), X,m (maximum specific growth rate), Xmax (maximum biomass concentration), tXmax (time to reach the maximum biomass concentration), YX/S (biomass yield from glucose), PX (biomass volumetric productivity), YE/X (specific yield factor).
For all parameters related to the synthesis of laccases (Table 4), superior results were observed in the test conducted on minimum values of 30% DO saturation (YE/S, PE, SALac and YE/X), quite higher than those found in the further conditions, highlighting the enzymatic productivity (PE) and specific yield factor (YE/X). In this test, also smaller biomass concentration was measured, showing that there is no proportional relationship between growth and synthesis of laccases, which also occurred with the concentration of total soluble proteins. For the biomass parameters, superior results were obtained in the test with higher growth (50% DO saturation).

DISCUSSION
Aerobic processes require a non-limiting amount of dissolved oxygen for microbial respiration. Oxygen supply directly affects biomass and is a crucial parameter for ensuring the adequate growth, cellular maintenance and production of metabolites. However, this gas is poorly soluble in aqueous media, so supplying oxygen to a culture is a complex task that is also affected by high levels of soluble nutrients [43].
Submerged fermentation of higher fungi is characterized by an increase in broth viscosity with time, either as a consequence of increased cell concentration, changes in microbial morphology, or because of the accumulation of extracellular products that alter the rheological characteristics of fermentation broth. After these changes, there will be several problems that should be considered and solved, especially with respect to oxygen supply. Oxygen affects cell growth, cellular morphology, nutrients uptake, and metabolite biosynthesis [32].
Oxygen, as a restricting nutrient, might cause severe alterations in the culture medium, positively or negatively interfering not only in microorganism growth but also in obtaining products of interests. The experiments of the present work show that high DO concentration in bioreactor does not favour laccases production, and its restriction, even if temporary, was significantly more beneficial to enzyme activity ( Figure  1 and 2). Therefore, it might be suggested that P. sajor-caju PS-2001, when under stress conditions due to lack or restriction of oxygen, tends to increase laccases production, in contrast to a condition of high O2 saturation, which negatively influences enzyme production.
In general, according to the results obtained, it was found that the tests conducted at pH between 4.5 and 7.0 favoured fungal growth, while tests carried out at fixed pH of 6.5 resulted in higher enzymatic levels However, among all the DO concentrations conditions tested, keeping DO at a minimum of 30% of saturation led to the highest laccases titles, regardless of the pH used. Shu and coauthors [44] observed that pH values of 4.0 and 5.0 are preferable for the cultivation of Agaricus blazei in stirred-tank bioreactor. For the ligninolytic fungus Trametes versicolor, Borràs and coauthors [45] reported that 4.5 is the ideal pH for growth. According to Thurston [7], when the fungus is grown on a medium whose pH is inadequately high for growth (around pH 5.0), laccases production is favoured.
Laccases are the main enzymes produced by P. sajor-caju PS-2001, although considerable levels of peroxidases have also been detected. However, MnP, LiP and VAO have shown low activity under any condition tested, as already noted in previous studies [28]. In experiments performed with the strain Pl-27 of Brazilian Archives of Biology and Technology. Vol.63: e20190015, 2020 www.scielo.br/babt P. sajor-caju, Fu and coauthors [46] have shown the fungus that produces MnP and laccases, but do not produce LiP in a medium containing glucose as substrate. The proteolytic activities showed no negative interference on the synthesis of laccases and the other phenol-oxidases quantified, showing relatively low levels in all cultivation (Tables 1 and 3).
The evaluations parameters for laccases and biomass presented in Tables 2 and 4 help to provide an understanding of the behaviour of the fungus under the conditions evaluated. Among these parameters, it is important to highlight the specific yield factor (YE/X), which proves that a high mycelial growth is not directly related to an increase in the synthesis of laccases, as verified, for example, in the cultivation at 30% of DO saturation and pH 6.5 ( Table 4).
The maximum specific growth rates (X,m) in the range 0,022 to 0,044 h -1 (Tables 2 and 4) are in agreement with values found for P. sajor-caju PS-2001 in previous studies conducted in stirred-tank reactor (STR). In those cultivation, carried out in a similar medium, with sucrose as a carbon source and gallic acid as enzyme inducer, replacing glucose and benzoic acid used in the present work, biomass concentration reached 5.2 g L -1 , which is greater than those observed in this work comparing all the conditions tested. However, the maximum laccases activity was only 40 U mL -1 , half the value obtained with growth conditions at 30% DO saturation and pH 6.5, which was after 80 U mL -1 (Table 3) [28].
As reported in literature, culture conditions such as impellers speed, airflow rate, pH, temperature, and medium composition directly influence fungal biomass growth and morphology as well as enzymatic activities [22,47,48]. In this study, initial aeration and agitation conditions were relatively gentle to prevent mycelial shearing, a damage frequently seen when filamentous fungi are cultivated in stirred-tank bioreactors. Such a situation was reported by Venkatadri and Irvine [49] for the cultivation of Phanerochaete chrysosporium, whose data showed a low production of ligninolytic enzymes in bioreactor, correlated with high impellers speed and consequent mycelial disruption. The negative effect caused by agitation (mechanical stress) on the production of fungal peroxidases and laccases was also observed in tests with Panus tigrinus in stirredtank bioreactor [50]. In addition, agitation intensity influences not only laccases activities in bioreactor but also biocatalyst stability [51].
Data from bioreactor experiments show that the highest DO levels used in this work -30 and 80% of saturationled to increasing fungal growth at pH between 4.5 and 7.0. Such results disagree with those obtained by Lee and coauthors [52] that reported higher concentration of mycelial biomass of Grifola frondosa under lower oxygenation of the cultivation medium. For Antrodia cinnamomea, it was observed that a high oxygen supply favours mycelial growth but the production of bioactive metabolites such as enzymes and extracellular polysaccharides [25] is inhibited. Therefore, these results suggest that there might be great variations in growth and metabolites production for different fungal species depending on the oxygen supply.
Results shown in Figures 1 and 2 suggest that laccases production by P. sajor-caju PS-2001 follows an associated kinetics model, where enzymatic synthesis occurs at the same time as microorganism growth, substrate consumption and decrease in DO and pH levels during primary metabolism [53]. However, studies with Volvariella volvacea report that enzymatic synthesis of this white-rot fungus is associated with secondary metabolism and it is positively regulated by the addition of up to 200 mol L -1 CuSO4 and several aromatic compounds [54].
Lai and coauthors [55] studied the effects of dissolved oxygen concentrations between 10 and 40% of saturation on the cultivation of Aspergillus terreus for obtaining secondary metabolites. According to these authors, increasing biomass concentrations were attained at DO of 30 and 40%. However, the high shear stress caused by the impeller speed necessary to maintain 40% of DO caused partial destruction of pellets and considerable reduction of production in comparison to the experiment in which 30% of DO was maintained. For the cultivation of Aspergillus niger, Li and coauthors [56] found that there was no inhibition of growth or nutrient consumption by the fungus, even at DO concentrations over 50% of saturation.
Stirred tank bioreactors have two particular problems that can be pointed out: the shearing of mycelium and the energy required to maintain the homogeneity of the medium. STR is normally used for enzyme production; however, the high-shear area due to the impellers, especially when a more intense agitation condition is required for achieving an adequate oxygen transfer to the liquid phase, can damage the microorganisms [57]. In spite of this, STR provides the attainment of superior results in terms of enzyme production when compared to bioreactors that allow a less shear-stressing environment, as observed by Fontana and coauthors [33] in the cultivation of Aspergillus oryzae for producing polygalacturonases in both mechanically stirred and airlift bioreactors. Meneghel and coauthors [58] evaluated cultures grown with limiting and non-limiting oxygen supplies of A. oryzae in STR for pectinases production, suggesting that the use of a growth-limiting medium can provide an effective oxygen supply to the microorganisms and excessively high impeller speeds that could damage the fungal hyphae.
Even today, STR are the most widely used cultivation systems with large applicability in industry and in laboratory scale, due to their great operational flexibility, being used in a large variety of bioprocesses such as the degradation of toxic compounds and the production of enzymes, biomass, polysaccharides and other microbial metabolites from different organisms [13,14,16,25,28,32,33,43,[49][50][51][55][56][57][58].

CONCLUSION
In conclusion, the results of this work make evident that dissolved oxygen concentration is a critical factor in the culture of P. sajor-caju PS-2001, with important effects not only on laccases production but also on fungal growth. Thus, it should be carefully assessed and controlled to achieve the best performance of the process. Data show that stress conditions by lack or restriction of oxygen supply might have positive effects on laccases production, in contrast to high availability of O2, which tends to negatively influence enzymatic production. Regardless of the pH used, the synthesis of laccases is favoured by maintaining the concentration of dissolved oxygen close to 30% of saturation, whereas superior DO levels favour fungal growth.