Lipolytic activity in submerged cultures of Issatchenkia orientalis

The ability of the yeast Issatchenkia orientalis CECT 10688 to secrete lipolytic activity in submerged culture was investigated. The yeast was grown in a complex medium supplemented with a fixed concentration of several lipidic compounds (triglycerides, fatty acids). Maximum enzyme activity around 70–80 U cm⁻³ was produced in cultures supplemented with tributyrin. An optimum tributyrin concentration of 10 g dm⁻³ was selected. Several surfactants were added to the cultures, but no significant increase in activity was detected. Finally, the effect of the type of carbon source on lipolytic enzyme production was studied. The best results were obtained with glucose and fructose (60–80 U cm⁻³), while rather low enzyme activity was found in cultures grown on lactose and maltose (about 20 U cm⁻³).     

Thermostable lipolytic enzymes production in batch and continuous cultures of Thermus thermophilus HB27

Several studies in laboratory-scale bioreactors are undertaken in order to verify the beneficial effect of thermal spring water in the culture medium of Thermus thermophilus HB27. Two bioreactor configurations, stirred tank and airlift, are investigated to determine the most suitable one to develop a continuous process. Water mineral composition affects the lipolytic enzyme secretion and growth of T. thermophilus HB27 in both bioreactor configurations. Furthermore, the lipolytic activity is strongly enhanced when stirred tank bioreactor is used. Moreover, operation in a stirred tank at an agitation rate of 650 rpm leads to the highest total lipolytic activity (intra- and extracellular enzyme) around 280 U/L after 32 h. Continuous cultures operating in the optimised conditions determined in batch cultures are carried out. It is noticeable that the stirred tank bioreactor was able to operate in a continuous flow mode without operational problems. In addition, the lipolytic activity obtained is about 2-fold higher than that attained in batch cultures.     

Scaling-up the production of thermostable lipolytic enzymes from Thermus aquaticus YT1

The lipolytic enzymes synthesized by Thermusaquaticus YT1 present extremely interesting properties of thermostability (more than 70% of activity after 12 days at 80°C and a half-life time of 1 h at 95°C), which point out the interest of proposing efficient strategies to successfully tackle the scale-up of the production process. In this study,viable scaling-up of the production process was implemented,and relevant aspects affecting the enzyme synthesis, such as the mineral composition of the culture medium, the aeration and the agitation have been evaluated.A strategy combining the modification of the culture medium and the aeration degree was also approached by adding perfluorocarbons, compounds which improve the availability of oxygen in the culture medium. An opposite response of biomass and lipolytic activity to the aeration conditions was found between scales (about 600 U L(-1) at high aeration levels in flask vs. 150 U L(-1) at high aeration rates in reactor), which further demonstrates the important role of the hydrodynamic conditions on the suitable development of the biological process. In all cases, the cultures were kinetically characterized and the Luedeking and Piret model turned out to be a valuable tool to conclude that the produced lipolytic enzyme is a growth-associated metabolite, no matter the medium and the scale.     

Immobilization of β-glucosidase in fixed bed reactor and evaluation of the enzymatic activity

Adsorption of β-glucosidase from almonds, an enzyme with big molecular size (130?kDa, 6.7?nm molecular diameter), on mesoporous SBA-15 silica in fixed bed column was studied. Previously, zeta potential analysis confirmed that the electrostatic interactions between β-glucosidase and SBA-15 were the driving force of the immobilization process. The maximum difference in the zeta potential was 25?mV at pH 3.5. Adsorption isotherm was classified as an L3 (Langmuir type 3) curve according to the Giles classification and fitted to a double Langmuir equation. The adsorbed amount in a fixed bed column was around 3.5 times higher than the amount reached in the adsorption in batch. In addition, the β-glucosidase was strongly immobilized on SBA-15 with only 7?% of leaching in the washing step with buffer solution. Immobilized β-glucosidase was catalytically active in a continuous process, reaching 100?% substrate conversion and maintaining this activity level for more than 10?h without deactivation of the enzyme. Adsorption-desorption isotherms at 77?K before and after the adsorption were carried out, concluding that the adsorption of β-glucosidase was produced blocking the pore mouth, so that a part of the enzyme penetrates inside and another part stays outside the pore.     

North Western Spain hot springs are a source of lipolytic enzyme-producing thermophilic microorganisms

Several hot springs in Galicia (North Western Spain) have been investigated as potential sources of lipolytic enzyme-producing thermophilic microorganisms. After isolating 12 esterase producing strains, 9 of them were assured to be true lipase producers, and consequently grown in submerged cultures, obtaining high extracellular activities by two of them. Furthermore, a preliminary partial characterization of the crude lipase, obtained by ultrafiltration of the cell-free culture supernatant, was carried out at several pH and temperature values. It is outstanding that several enzymes turned out to be multiextremozymes, since they had their optimum temperature and pH at typical values from thermoalkalophiles. The thermal stability in aqueous solution of the crude enzymes was also assayed, and the influence of some potential enzyme stabilizing compounds was tested. Finally, the viability of the selected microorganisms has been demonstrated at bioreactor scale.     

Lipolytic enzyme production by Thermus thermophilus HB27 in a stirred tank bioreactor

In this study, lipolytic enzyme production by Thermus thermophilus HB27 at bioreactor scale has been investigated. Cultivation was performed in a 5-L stirred tank bioreactor in discontinuous mode, at an agitation speed of 200 rpm. Different variables affecting intra- and extra-cellular lipolytic enzyme production such as culture temperature and aeration rate have been analysed. The bacterium was able to grow within the temperature range tested (from 60 to 70 °C) with an optimum value of 70 °C for intra- and extra-cellular lipolytic enzyme production.On the other hand, various aeration levels (from 0 to 2.5 L/min) were employed. A continuous supply of air was necessary, but no significant improvement in biomass or enzyme production was detected when air flow rates were increased above 1 L/min. Total lipolytic enzyme production reached a maximum of 167 U/L after 3 days, and a relatively high concentration of extra-cellular activity was detected (40% of the total amount). Enzyme yield was around 158 U/g cells. Moreover, it is noteworthy that the lipolytic activity obtained operating at optimal conditions (70 °C and air flow of 1 L/min) was about five-fold higher than that attained in shake flask cultures     

Optimization of maltodextrin hydrolysis by glucoamylase in a batch reactor

The hydrolysis of maltodextrins (10 DE) by glucoamylase was studied in a batch reactor at temperatures between 40 and 80 degrees C and substrate concentration range from 17 to 300 kg/m(-3). The experimental data were fitted to a model including thermal deactivation of the enzyme. In the model, the reaction rate was correlated with an extended Michaelis-Menten equation including inhibition by product, and the thermal deactivation of glucoamylase was fitted with a first-order reaction. The dependence of rate parameters on temperature was correlated using the Arrhenius equation. The differential equation of the model was integrated and the optimal enzyme demand and temperature were determined for isothermal operation.     

Screening Botryosphaeria species for lipases: Production of lipase by Botryosphaeria ribis EC-01 grown on soybean oil and other carbon sources

Nine isolates of Botryosphaeria spp. were screened for lipases when cultivated on eight different plant seed oils and glycerol, and all produced lipases. Botryosphaeria ribis EC-01 produced highest lipase titres on soybean oil and glycerol, while eight isolates of Botryosphaeria rhodina produced significantly lower enzyme titres. B. ribis EC-01 produced lipase when grown on different fatty acids, surfactants, carbohydrates and triacylglycerols, with highest enzyme titres produced on Triton X-100-emulsified stearic (316.7 U/mL), palmitic (283.5 U/mL) and oleic (247.4 U/mg) acids, and soybean oil (105.6 U/mL), as well as castor oil (191.2 U/mg); an enhancement of 9-fold over soybean oil-grown cultures. Glycerol was also a good substrate for lipase production. The crude lipase extract was optimally active at pH 8.0 and 55 °C, stable between 30 and 55 °C and pH 1–10, and tolerant to 50% (v/v) glycerol, methanol and ethanol. The crude lipase showed affinity for substrates of short, average and long-chain fatty acids (different esters of p-nitrophenol and triacylglycerols). Zymograms developed with 4-methylumbelliferyl-butyrate showed two bands of lipolytic activity at 45 and 15 kDa. This is the first report on the production of lipases by B. ribis grown on these different carbon sources.     

Standardization of assay procedure and some properties of ribonuclease fromaspergillus candidus

Screening of several fungal cultures resulted in the selection of an isolate of Aspergillus candidus which produced a considerable around of RNa-degrading enzyme in both surface and submerged methods of cultivation. The conditions for the assay of the RNAase were standardized at pH 4.5, 55 degrees C and using 0.25% yeast RNA as substrate. The enzyme was stable at pH 5.2. EDTA was found to activate the enzyme slightly. at temperatures 50-60 degrees C there was considerable loss in enzyme activity which was traced to the presence of a contaminating protease which presumably degraded the RNAase optimally at this temperature. The protease could be preferentially inactivated at or above 75 degrees C. The crude enzyme, in addition to RNAase was found to possess DNAase, nonspecific phosphodiesterase and 3'- and 5'-phosphomonoesterase activities.     

Comparative study of amylolytic enzymes production byAspergillus niger in liquid and solid-state cultivation

Summary Amylolytic enzymes produced by a strain ofAspergillus niger cultivated on cassava starch in liquid or solid culture were found to be mainly glucoamylases. For the same initial amount of substrate, the glucoamylase activity increased even after 60 h of culture on solid medium whereas it decreased in liquid culture. Some characteristics of the amylases produced in both culture conditions were compared. The pH optima for enzymes produced in solid and liquid cultures were 4.5 and 5.0 respectively. Glucoamylase synthetized in solid cultures was significantly more thermostable than that from liquid culture and was maximally active at 70°C compared to 50°C for the enzyme from liquid cultures. The Km values expressed as mg soluble starch/100 ml were 0.1% for crude enzyme from solid culture and 0.057% for crude enzyme from liquid culture.     

Selection of pH buffers for use in conductimetric microbiological assays

The lipolytic floras of 36 raw milk samples showing lipolytic defects were dominated by pseudomonads. Representative lipolytic isolates were selected and tested for growth, lipase activity and lipolysis in ultra-heat-treated milk at temperatures ranging from 5° to 30°C. Pseudomonas fluorescens was the most frequently encountered species but Ps. fragi was found to cause more severe lipolytic defects in both single and mixed strain milk cultures. A representative strain of Ps. fragi multiplied faster in cold-stored milk than did three representative strains of Ps. fluorescens. The lipases produced by Ps. fragi strains were more heat-stable than those produced by Ps. fluorescens strains.     

Growth of lipolytic psychrotrophic pseudomonads in raw and ultra-heat-treated milk

The lipolytic floras of 36 raw milk samples showing lipolytic defects were dominated by pseudomonads. Representative lipolytic isolates were selected and tested for growth, lipase activity and lipolysis in ultra-heat-treated milk at temperatures ranging from 5 degrees to 30 degrees C. Pseudomonas fluorescens was the most frequently encountered species but Ps. fragi was found to cause more severe lipolytic defects in both single and mixed strain milk cultures. A representative strain of Ps. fragi multiplied faster in cold-stored milk than did three representative strains of Ps. fluorescens. The lipases produced by Ps. fragi strains were more heat-stable than those produced by Ps. fluorescens strains.     

Strategies for utilisation of food-processing wastes to produce lipases in solid-state cultures of Rhizopus oryzae

The aim of the present study was to investigate the feasibility of several food-processing wastes as support substrate for lipolytic enzymes production by the fungus Rhizopus oryzae under solid-state conditions. Different experiments were conducted to select the variables that allow obtaining high levels of lipolytic enzyme activity. In particular, the use of inert and non-inert solid materials and lipidic and surfactant compounds was evaluated. It was observed that the addition of Triton X-100 together with barley bran involved lipolytic production values tenfold higher than the cultures exclusively grown on an inert support. In addition, from preliminary thermoinactivation kinetics studies, it was concluded that the strategy proposed in this investigation entails another benefit in terms of resistance of the produced enzymes against thermoinactivation.     

Strategies for improving extracellular lipolytic enzyme production by Thermus thermophilus HB27

In Thermus thermophilus HB27 cultures the localisation of lipolytic activity is extracellular, intracellular and membrane bound, with low percentage for the former. Therefore, the extracellular secretion must be increased in order to simplify the downstream process and to reduce the economic cost. This study focuses on the design of an innovative operational strategy to increase extracellular lipolytic enzyme production by T. thermophilus HB27 at bioreactor scale. In order to favour its secretion, the effect of several operational variables was evaluated. Among them, the presence of oils in the culture medium leads to improvements in growth and lipolytic enzyme activity. Sunflower oil is the most efficient inducer showing better results when added after 10 h of growth. On the other hand, although surfactants lead to an almost complete inhibition of growth and lipolytic enzyme production, their addition along the culture could affect the location of the enzyme. Thus, by addition of surfactants at the stationary phase, a release of intracellular and membrane enzyme which increases the extracellular enzyme proportion is detected. Based on these results, strategies with successive addition of oil and surfactant in several culture phases in shake flask are developed and verified in a laboratory scale stirred tank bioreactor.     

Prediction of continuous reactors performance based on batch reactor deactivation kinetics data of immobilized lipase

Experiments on deactivation kinetics of immobilized lipase enzyme fromCandida cylindracea were performed in stirred batch reactor using rice bran oil as the substrate and temperature as the deactivation parameter. The data were fitted in first order deactivation model. The effect of temperature on deactivation rate was represented by Arrhenius equation. Theoretical equations were developed based on pseudo-steady state approximation and Michaelis-Menten rate expression to predict the time course of conversion due to enzyme deactivation and apparent half-life of the immobilized enzyme activity in PFR and CSTR under constant feed rate policy for no diffusion limitation and diffusion limitation of first order. Stability of enzyme in these continuous reactors was predicted and factors affecting the stability were analyzed.     

Acid phosphatase deactivation by a series mechanism

Acid phosphatase (E.C.3.1.3.2.) thermal deactivation at pH 3.77 has been investigated by monitoring the enzyme activity as a function of time in the hydrolysis of p-nitrophenyl phosphate. The experimental curves obtained show a two-slope behavior in a log (activity)versus-time plot, which indicates that deactivation occurs via a complex mechanism. From the dependence of the kinetic parameters on both deactivation and hydrolysis temperatures, it is inferred that the deactivation mechanism involves intermediate, temperature-dependent, less-active forms of the enzyme. This interpretation is confirmed by the results of additional tests in which the temperature was suddenly changed during the deactivation process.     

Enzymatic hydrolysis of soluble starch with an alpha-amylase from Bacillus licheniformis

The enzymatic hydrolysis of soluble starch with an alpha-amylase from Bacillus licheniformis (commercial enzyme Termamyl 300 L Type DX) have been experimentally studied at pH 7.5, within the temperature range of 37-75 degrees C, at initial substrate concentrations of between 0.25 and 2.00 g/L, and enzyme concentrations of between 0.575 x 10(-4) and 13.8 x 10(-4) g/L. To follow the reaction a procedure based on the iodometric method for measuring alpha-amylase activity was used. The kinetics of the enzymatic hydrolysis was fitted to the Michaelis-Menten equation using the integral method, taking into account that the thermal deactivation of the enzyme follows a second-order kinetic. These parameters were fitted to the Arrhenius equation obtaining activation energies of 24.4 and 41.7 kJ/mol and preexponential factors of 734.9 g/L and 1.74 x 10(8) min(-1) for K(M) and k, respectively.     

Isolation and Screening of Alkaline Lipase-producing Fungi from Brazilian Savanna Soil

Summary Fifty-nine lipase-producing fungal strains were isolated from Brazilian savanna soil by employing enrichment culture tecniques. An agar plate medium containing bile salts and olive oil emulsion was employed for isolating and growing fungi in primary screening assay. Twenty-one strains were selected by the ratio of the lipolytic halo radius and the colonies radius. Eleven strains were considered good producers under conditions of submerged liquid fermentation (shaken cultures) and solid-state fermentation. The most productive strain, identified as Colletotrichum gloesporioides, produced 27,700 U/l of lipase under optimized conditions and the crude lipase preparation was capable of hydrolysing a broad range of substrates including lard, natural oils and tributyrin.     

Visualization by freeze fracture, in vitro and in vivo, of the products of fat digestion

The technique of freeze fracture was used to visualize triglyceride (TG) hydrolysis and the production of lipolytic products (LPs) in vitro and in vivo in the presence of bile salts (BS). Three systems were investigated: pure lipolytic products (oleic acid and monoolein) in the presence of a pure bile salt (taurodeoxycholate (TDC)), lipolytic products produced from TG by pancreatic lipase in the presence of a variety of bile salts, and lipolytic products produced in the intestine of the killifish, Fundulus heteroclitus, after fat feeding. In vitro, lamellae (4-5 nm thick with 0-8-nm water spacings) appeared on the surface of TG droplets in all preparations with LP/BS molar ratios of 1.5 or greater and spherical vesicles (diameter range, 20-130 nm) were produced from these lamellae. With model killifish bile (taurocholate-cholate 1:1) at LP/BS ratios between 1.5 and 4, homogeneous vesicles or particles (mean diameter, 23.8 nm) were produced by lipase at pH 6.9. In vivo, lamellar product phases also occurred after fat feeding. The smallest visible LP/BS structures by freeze fracture electron microscopy were approximately 20 nm globular particles. Large disc-shaped micelles either were not present or were below the resolution limit of the replica (approximately 10 nm). The dominant aggregated lipolytic product phase was composed of multiple layers of rough-textured lamellae. No evidence of cubic structure was seen. These results show that lamellar and vesicular lipolytic product phases can be intermediates in intestinal fat digestion. However, no evidence for the direct endocytotic absorption of these product phases by the intestinal microvillus membrane was found.     

Enzymatic hydrolysis of cellulose in aqueous two-phase systems. II. Semicontinuous conversion of a model substrate, solka floc BW 200

A model substrate, Solka Floc BW 200, was semicontinuously hydrolyzed in an aqueous two-phase system based on crude dextran and polyethylene glycol over a period of more than 450 h. With an initial concentration of 75 g/L and intermittent addition of cellulose an average concentration of 50 g/L sugar was semicontinuously produced at dilution rates of 0.006-0.012 h(-1). The conversion of substrate varied between 49 and 66%. The enzyme consumption measured as FPU/g reducing sugar (RS) produced could be reduced by a factor two when compared to a batch process since, in the aqueous two phase system investigated, the enzyme could be recycled two times.