An improved method of lipase preparation incorporating both solvent treatment and immobilization onto matrix

A simple and effective preparation of lipases for use in organic solvents is hereby proposed. Lipases in aqueous solution were treated with isopropanol, immediately followed by immobilization onto a commercially available macroporous resin CRBO2 (crosslinked polystyrene with N-methylglucamine as a functional group). The dual modification of lipases by (1) isopropanol treatment and (2) immobilization improved the activity and stability of lipases more significantly than either of the two treatments alone. The degree of lipase activation was dependent on isopropanol–buffer (v/v) ratio and the source of lipase used. Among the lipases tested, Rhizopus oryzae lipase was more significantly activated. The maximum specific activity of R. oryzae lipase after dual modification was 94.9 mmol h⁻¹ g⁻¹, which was, respectively, 3.3-, 2.5- and 1.5-fold of untreated free, untreated immobilized and treated free lipases. The conformations of the treated and untreated free lipases were investigated by circular dichroism (CD) measurement. Changes in the far- and near-UV CD spectra of lipase indicate that lipase activation is accompanied by changes in secondary and tertiary structures of lipases. The increase in negative molar elipticity at 222 nm suggests that the α-helical content of lipase increase after pretreatment.     

Evaluation of distant carbon sources in biosurfactant production by a gamma ray-induced Pseudomonas putida mutant

Pseudomonas putida 33 wild strain, subjected to gamma ray mutagenesis and designated as P. putida 300-B mutant was used as microbial rhamnolipid-producer by using distant carbon sources (viz. hydrocarbons, waste frying oils ‘WFOs’, vegetable oil refinery wastes and molasses) in the minimal media under shake flask conditions. The behavior of glucose as co-substrate and growth initiator was examined. The 300-B mutant strain showed its ability to grow on all the substrates tested and produced rhamnolipid surfactants to different extents however; soybean and corn WFOs were observed to be preferred carbon sources followed by kerosene and paraffin oils, respectively. The best cell biomass (3.5 g l⁻¹) and rhamnolipids yield (4.1 g l⁻¹) were obtained with soybean WFO as carbon source and glucose as growth initiator under fed-batch cultivation showing an optimum specific growth rate (μ) of 0.272 h⁻¹, specific product yield (q_p) of 0.318 g g⁻¹ h and volumetric productivity (P_V) of 0.024 g l⁻¹ h. The critical micelle concentration of its culture supernatant was observed to be 91 mg rhamnolipids l⁻¹ and surface tension as 31.2 mN m⁻¹.     

Laccase mediator system for activation of agarose gel: Application for immobilization of proteins

Cross-linked Sepharose beads were treated with laccase–TEMPO system for oxidation of the primary alcohol groups on the sugar moieties. Optimal activation conditions using Trametes versicolor laccase were at pH 5 and 22 °C, giving an aldehyde content of 55 μmol g⁻¹ Sepharose with 28 units g⁻¹ of laccase and 12.5 mM TEMPO. The activated Sepharose was used for immobilization of trypsin as model protein. Highest degree of immobilization was obtained at pH 10.5 but the activity yield was only 31% of that loaded on the gel. The yield of gel bound trypsin activity was increased to 76% (corresponding to about 43 U g⁻¹ Sepharose) when the immobilization was performed in the presence of trypsin inhibitor, benzamidine. The immobilization yields were comparable to that obtained on the matrix activated using sodium periodate (containing 72 μmol aldehyde per g Sepharose). Recycling and storage of the immobilized trypsin preparations showed high stability of the enzyme bound to laccase–TEMPO activated gel.     

Proposed kinetic mechanism of the production of biodiesel from palm oil using lipase

Experimental determination of the separate effects of palm oil and methanol concentrations on the rate of their enzymatic transesterification was used to propose suitable mechanismic steps and to test the generated kinetic model. The reaction took place in n-hexane organic medium and the lipase used was from Mucor miehei. At a constant methanol concentration of 300 mol m⁻³, it was found that, initially as the palm oil concentration increased, the initial reaction rate increased. However, the initial rate dropped sharply at substrate concentrations larger than 1250 mol m⁻³. Similar behaviour was observed for methanol concentration effect, where at a constant substrate concentration of 1000 mol m⁻³, the initial rate of reaction dropped at methanol concentrations larger than 3000 mol m⁻³. Ping Pong Bi Bi mechanism with inhibition by both reactants was adopted as it best explains the experimental findings. A mathematical model was developed from a proposed kinetic mechanism and was used to identify the regions where the effect of inhibition by both substrates arised. The proposed model equation is essential for predicting the rate of methanolysis of palm oil in a batch or a continuous reactor and for determining the optimal conditions for biodiesel production.     

Immobilization of lipase in organic solvent in the presence of fatty acid additives

In this study porcine pancreatic lipase (PPL) was covalently immobilized on cross-linked polyvinyl alcohol (PVA) in organic media in the presence of fatty acid additives in order to improve its immobilized activity. The effects of fatty acid additions to the immobilization media were investigated choosing tributyrin hydrolysis in water and ester synthesis by immobilized PPL in n-hexane. Various fatty acids which are also the substrates of lipases in esterification reactions were used as active site protecting agents during the immobilization process in an organic solvent. The obtained results showed that covalent immobilization carried out in the presence of fatty acids as protective ligands improved the hydrolytic and esterification activity of immobilized enzyme. A remarkable increase in activity of the immobilized PPL was obtained when octanoic acid was used as an additive and the hydrolytic activity was increased from 5.2 to 19.2 μmol min⁻¹ mg⁻¹ as compared to the non-additive immobilization method. With the increase of hydrolytic activity of immobilized lipase in the presence of octanoic acid, in an analogous manner, the rate of esterification for the synthesis of butyl octanoate was also increased from 7.3 to 26.3 μmol min⁻¹ g⁻¹ immobilized protein using controlled thermodynamic water activities with saturated salt solutions. In addition, the immobilized PPL activity was maintained at levels representing 63% of its original activity value after 5 repeated uses. The proposed method could be adopted for a wide variety of other enzymes which have highly soluble substrates in organic solvent such as other lipases and esterases.     

Immobilized lipase on macroporous polystyrene modified by PAMAM-dendrimer and their enzymatic hydrolysis

The novel enzyme carrier, polyamidoamine (PAMAM) dendrimers modified macroporous polystyrene, has been synthesized by Michael addition and firstly used in the immobilization of porcine pancreas lipase (PPL) effectively by covalent attachment. The resulting carrier was characterized with the Fourier transform infrared spectra (FT-IR), scanning electron microscopy (SEM), elemental analysis and thermogravimetric (TG) analysis. Meanwhile, the amount of immobilized lipase was up to 100 mg g⁻¹ support and the factors related with the enzyme activity were investigated. The immobilization of the PPL improved their performance in wider ranges of pH and temperature. Thermal stability of the immobilized lipase also increased dramatically in comparison with the free ones and the immobilized lipase exhibited a favorable denaturant tolerance. As a biocatalyst, the immobilized lipase for batch hydrolysis of olive oil emulsion retained 85% activity after 10 times of recycling. This well-reusability of immobilized lipase was very valuable and meaningful in enzyme technology.     

Characterization of the lipase immobilized on Mg–Al hydrotalcite for biodiesel

Immobilization of Saccharomyces cerevisiae lipase by physical adsorption on Mg–Al hydrotalcite with a Mg/Al molar ratio of 4.0 led to a markedly improved performance of the enzyme. The immobilized lipase retained activity over wider ranges of temperature and pH than those of the free lipase. The immobilized lipase retained more than 95% relative activity at 50 °C, while the free lipase retained about 88%. The kinetic constants of the immobilized and free lipases were also determined. The apparent activation energies (E_a) of the free and immobilized lipases were estimated to be 6.96 and 2.42 kJ mol^?1, while the apparent inactivation energies (E_d) of free and immobilized lipases were 6.51 and 6.27 kJ mol^?1, respectively. So the stability of the immobilized lipase was higher than that of free lipase. The water content of the oil must be kept below 2.0 wt% and free fatty acid content of the oil must be kept below 3.5 mg KOH g [oil]^?1 in order to get the best conversion. This immobilization method was found to be satisfactory to produce a stable and functioning biocatalyst which could maintain high reactivity for repeating 10 batches with ester conversion above 81.3%.     

Tween 80 influences the production of intracellular lipase by Schizochytrium S31 in a stirred tank reactor

Marine microorganisms are a potential source of enzymes with structural stability, high activity at low temperature and unique substrate selectivity. Thraustochytrids are marine heterotrophic microbes, well known for the production of omega-3 fatty acids. In this study the effect of Tween 80 as a carbon source was investigated with regard to biomass, lipase and lipid productivity in Schizochytrium sp. S31. Tween 80 (1%) and 120 h of incubation were the optimum condition period for biomass, lipid and lipase productivity in a stirred tank reactor. The yields obtained were 0.9 g L⁻¹ of biomass, 300 mg g⁻¹ of lipid and 39 U/g of lipase activity. Sonication was optimised in terms of time and acoustic power to maximise the yield of extracted lipase. The extracted lipase from Schizochytrium S31 was observed to hydrolyse long chain polyunsaturated fatty acids DHA and EPA.     

Optimization studies to develop a low-cost medium for production of the lipases of Rhizopus microsporus by solid-state fermentation and scale-up of the process to a pilot packed-bed bioreactor

A low-cost lipase preparation is required for enzymatic biodiesel synthesis. One possibility is to produce the lipase in solid-state fermentation (SSF) and then add the fermented solids (FS) directly to the reaction medium for biodiesel synthesis. In the current work, we scaled up the production of FS containing the lipases of Rhizopus microsporus. Initial experiments in flasks led to a low-cost medium containing wheat bran and sugarcane bagasse (50:50 w/w, dry basis), supplemented only with urea. We used this medium to scale-up production of FS, from 10 g in a laboratory column bioreactor to 15 kg in a pilot packed-bed bioreactor. This is the largest scale yet reported for lipase production in SSF. During scale-up, the hydrolytic activity of the FS decreased 57%: from 265 U g⁻¹ at 18 h in the laboratory bioreactor to 113 U g⁻¹ at 20 h in the pilot bioreactor. However, the esterification activity decreased by only 14%: from 12.1 U g⁻¹ to 10.4 U g⁻¹. When the FS produced in the laboratory and pilot bioreactors were dried and added directly to a solvent-free reaction medium to catalyze the esterification of oleic acid with ethanol, both gave the same ester content, 69% in 48 h.     

Immobilization of lipase on epoxy-activated Purolite® A109 and its post-immobilization stabilization

In this study, Purolite^® A109, polystyrenic macroporous resin, was used as immobilization support due to its good mechanical properties and high particle diameter (400 μm), which enables efficient application in enzyme reactors due to lower pressure drops. The surface of support had been modified with epichlorhydrine and was tested in lipase immobilization. Optimized procedure for support modification proved to be more efficient than conventional procedure for hydroxy groups (at 22 °C for 18 h), since duration of procedure was shortened to 40 min by performing modification at 52 °C resulting with almost doubled concentration of epoxy groups (563 μmol g⁻¹). Lipase immobilized on epoxy-modified support showed significantly improved thermal stability comparing to both, free form and commercial immobilized preparation (Novozym^® 435). The highest activity (47.5 IU g⁻¹) and thermal stability (2.5 times higher half-life than at low ionic strength) were obtained with lipase immobilized in high ionic strength. Thermal stability of immobilized lipase was further improved by blocking unreacted epoxy groups on supports surface with amino acids. The most efficient was treatment with phenylalanine, since in such a way blocked immobilized enzyme retained 65% of initial activity after 8 h incubation at 65 °C, while non-blocked derivative retained 12%.     

Ability of Vasconcellea × heilbornii lipase to catalyse the synthesis of alkyl esters from vegetable oils

Lipase-catalysed synthesis of alkyl esters is regarded as a potential alternative to chemical catalysis. Owing to its availability as a waste material from the babaco fruit production, its strong lipolytic activity and its natural immobilization, the dried latex of Vasconcellea × heilbornii appears as a good candidate to produce alkyl esters. The ability and performance of this lipase to catalyse the alcoholysis of sunflower oil with various primary alcohols was evaluated in a solvent-free system. A linear correlation between the final reaction rate and the alcohol polarity was established. For methanolysis, the influence of substrates ratio on final conversion rate was studied at different temperatures. At 30 °C, the lipase was inactivated by shaking in a mixture containing more than 0.5 molar equivalents of methanol; the minimum methanol concentration for enzyme deactivation increased with temperature. Moreover, for a 0.5:1 methanol/TAG molar ratio, conversion rates of 73, 66 and 55% were obtained at 30, 40 and 55 °C respectively, showing that the increase of temperature diminished the final methanolysis conversion rate. These facts were associated to the miscibility of methanol in oil and to the thermodynamic state of the medium. To overcome the inactivation of the lipase by methanol, alcoholysis was carried out by fractionated addition of methanol. In those conditions, Vasconcellea × heilbornii latex could catalyse the conversion of 70% of sunflower TAGs in methyl esters at 30 °C.     

Volatile fatty acids accumulation and rhamnolipid generation in situ from waste activated sludge fermentation stimulated by external rhamnolipid addition

The solubilization and acidification of waste activated sludge (WAS) were apparently enhanced by external rhamnolipid (RL) addition. The maximum solute carbohydrate concentrations increased linearly from 48 ± 5 mg COD L⁻¹ in the un-pretreated WAS (blank) to 566 ± 19 mg COD L⁻¹, and protein increased from 1050 ± 8 to 3493 ± 16 mg COD L⁻¹ at RL dosage of 0.10 g g⁻¹ TSS. The highest VFAs concentration peaked at 3840 mg COD L⁻¹ at RL dosage of 0.04 g g⁻¹ TSS, which was 4.24-fold higher than the blank test. RL was generated in situ during WAS fermentation when external RL was added. It was detected that RL concentration was increased from initial 880 ± 92 mg L⁻¹ to 1312 ± 7 mg L⁻¹ at the end of 96 h with RL dosage of 0.04 g g⁻¹ TSS, which was increased to 1.49-fold. Meanwhile, methane production was notably reduced to a quite low level of 2.0 mL CH₄ g⁻¹ VSS, showing effective inhibition of methanogens by RL (58.8 mL CH₄ g⁻¹ VSS in the blank). In addition, the activity of hydrolytic enzymes (protease and α-glucosidase) was enhanced accordingly. VFAs accumulation and RL generation in situ demonstrated that the additional RL substantially performed enhanced biological effects for waste activated sludge fermentation.     

Insecticidal properties of Pimpinella anisum essential oils against the Culex quinquefasciatus and the non-target organism Daphnia magna

The efficacy of an essential oil obtained from Pimpinella anisum fruits and its major compound, trans-Anethole, was tested on the eggs, larvae and adults of Culex quinquefasciatus. While causing no significant mortality on eggs, other tested stages were very sensitive to the essential oil and trans-Anethole. LC₅₀ for the 2nd to 4th instar larvae was estimated as 26–27 μL·L^− 1 and 15–19 μL·L^− 1 for the essential oil and trans-Anethole, respectively. As for the essential oil applied on adults, LC(LD)₅₀ was estimated as 9.3 μL mL^− 1 (spray test), 1.9 μL L^− 1 (fumigation test) and 0.6 μg cm^− 2 (tarsal test), and for trans-Anethole as 8.1 μL mL^− 1 (spray test), 2.1 μL L^− 1 (fumigation test) and 0.4 μg cm^− 2 (tarsal test). The time needed to achieve 50% mortality after application of LC(LD)₉₉ of the essential oil was significantly different; for example, in larvicidal assays it ranged from 15 to 235 min depending on the larval instar, and from 9 to 180 min when applied to adults, depending on the mode of application. It was also found that temperature had an important effect on the larvicidal efficacy of the essential oil, and oviposition deterrent activity was studied.The essential oil and trans-Anethole were toxic for Daphnia magna (62–92% mortality) and significantly reduced its fertility at high concentrations (35–50 μL mL^− 1) and long exposure (48 h). However, no negative effect on Daphnia mortality or fertility was found at shorter exposure times (6 h) and/or lower concentrations (20 μL mL^− 1).Based on the results of this study, we can recommend the essential oil from P. anisum as a suitable active substance for potential botanical insecticides.     

Site-directing an intense multipoint covalent attachment (MCA) of mutants of the Geobacillus thermocatenulatus lipase 2 (BTL2): Genetic and chemical amination plus immobilization on a tailor-made support

Immobilized enzymes are preferred over their soluble counterparts due to their robustness in harsh industrial processes; the most stable enzyme derivatives are often produced through multipoint covalent attachment (MCA). However, most enzymes are unable to establish optimal MCA to electrophile-type supports given the heterogeneous distribution and/or low content of primary amino groups on their surfaces; this restricts both the diversity of areas prone to react and the number of attachments to the support. To overcome this we propose combining site-directed immobilization and protein engineering to increase the number of bonds between a specific enzyme surface and a tailor-made support. We applied this novel strategy to engineered mutants of the lipase 2 from Geobacillus thermocatenulatus with one Cys exposed residue, that after genetic amination and/or chemical amination, were immobilized on glyoxyl-disulfide support using a site-directed MCA protocol. Two highly stabilized derivatives of chemically aminated lipase variants, in which site-directed MCA implied the surrounding surface of residues Cys344 or Cys40, were produced: the first one was 2.4-fold more productive than the reference derivative (648 g of hydrolyzed ester); the second derivative was 40% more selective (EPA/DHA molar ratio) and as active (1 μmol g catalyst⁻¹ min⁻¹) as the reference in the production of PUFAs.     

Improvement in lipase-catalyzed methanolysis of triacylglycerols for biodiesel production using a solvent engineering method

A solvent engineering strategy was applied to the lipase-catalyzed methanolysis of triacylglycerols for biodiesel production. The effect of different pure organic solvents and co-solvent mixtures on the methanolysis was compared. The substrate conversions in the co-solvent mixtures were all higher than those of the corresponding pure organic solvents. Further study showed that addition of co-solvent decreased the values of |log P_interface − log P_substrate| and thus led to a faster reaction. The more the values of |log P_interface − log P_substrate| decreased, the faster the reaction proceeded and the higher the conversion attained. Different co-solvent ratio was further investigated. The co-solvent mixture of 25% t-pentanol:75% isooctane (v/v) was optimal, with which both the negative effects caused by excessive methanol and by-product glycerol could be eliminated. There was no obvious loss in lipase activity even after being repeatedly used for 60 cycles (720 h) with this co-solvent mixture as reaction medium. Other lipases and lipase combinations can also catalyze methanolysis in this co-solvent mixture. Furthermore, other vegetable oils were also explored for biodiesel production in this co-solvent mixture and it had been found that this co-solvent mixture media has extensive applicability.     

Immobilization of acidic lipase derived from Pseudomonas gessardii onto mesoporous activated carbon for the hydrolysis of olive oil

Mesoporous activated carbon (MAC) derived from rice husk is used for the immobilization of acidic lipase (ALIP) produced from Pseudomonas gessardii. The purified acidic lipase had the specific activity and molecular weight of 1473 U/mg and 94 kDa respectively. To determine the optimum conditions for the immobilization of lipase onto MAC, the experiments were carried out by varying the time (10–180 min), pH (2–8), temperature (10–50 °C) and the initial lipase activity (49 × 10³, 98 × 10³, 147 × 10³ and 196 × 10³ U/l in acetate buffer). The optimum conditions for immobilization of acidic lipase were found to be: time—120 min; pH 3.5; temperature—30 °C, which resulted in achieving a maximum immobilization of 1834 U/g. The thermal stability of the immobilized lipase was comparatively higher than that in its free form. The free and immobilized enzyme kinetic parameters (K_m and V_max) were found using Michaelis–Menten enzyme kinetics. The K_m values for free enzyme and immobilized one were 0.655 and 0.243 mM respectively. The immobilization of acidic lipase onto MAC was confirmed using Fourier Transform-Infrared Spectroscopy, X-ray diffraction analysis and scanning electron microscopy.     

Amperometric biosensor based on a site-specific immobilization of acetylcholinesterase via affinity bonds on a nanostructured polymer membrane with integrated multiwall carbon nanotubes

Acetylcholinesterase (AChE) was immobilized on chemically modified poly-(acrylonitrile-methyl-methacrylate-sodium vinylsulfonate) membranes in accordance with three different methods, the first of which involved random enzyme immobilization via glutaraldehyde, the second one—site-specific enzyme immobilization via glutaraldehyde and Concanavalin A (Con A) and the third method—modified site-specific enzyme immobilization via glutaraldehyde in the presence of a mixture of multiwall carbon nanotubes and albumin (MWCNs + BSA), glutaraldehyde and Con A. Preliminary tests for the activity of immobilized AChE were carried out using these three methods. The third method was selected as the most efficient one for the immobilization of AChE and the prepared enzyme carriers were used for the construction of amperometric biosensors for the detection of acetylthiocholine (ATCh).A five level three factorial central composite design was chosen to determine the optimal conditions for the enzyme immobilization with three critical variables: concentration of enzyme, Concanavalin A and MWCNs. The design illustrated that the optimum values of the factors influencing the amperometric current were C_E: 70 U mL⁻¹; C_{Con A}: 1.5 mg mL⁻¹ and C_MWCN: 11 mg mL⁻¹, with an amperometric current 0.418 μA. The basic amperometric characteristics of the constructed biosensor were investigated. A calibration plot was obtained for a series of ATCh concentrations ranging from 5 to 400 μM. A linear interval was detected along the calibration curve from 5 to 200 μM. The correlation coefficient for this concentration range was 0.995. The biosensor sensitivity was calculated to be 0.065 μA μM⁻¹ cm⁻². The detection limit with regard to ATCh was calculated to be 0.34 μM. The potential application of the biosensor for detection and quantification of organophosphate pesticides was investigated as well. It was tested against sample solutions of Paraoxon. The biosensor detection limit was determined to be 1.39 × 10⁻¹² g L⁻¹ of Paraoxon, as well as the interval (10⁻¹¹ to 10⁻⁸ g L⁻¹) within which the biosensor response was linearly dependant on the Paraoxon concentration. Finally the storage stability of the enzyme carrier was traced for a period of 120 days. After 30-day storage the sensor retained 76% of its initial current response, after 60 days—68% and after 120 days—61%.     

Optimized endodextranase-epoxy CIM® disk reactor for the continuous production of molecular weight-controlled prebiotic isomalto-oligosaccharides

An epoxy-activated monolithic Convective Interaction Media (CIM^®) disk was used for the immobilization of endodextranase D8144 from Penicillium sp. (EC 3.2.1.11) in order to produce on-line isomalto-oligosaccharides (IMOs) from Dextran T40. Enzymatic parameters, molecular weight of IMOs and performance of the IMmobilized Enzymes Reactor (IMER) were investigated. The immobilization yield of enzymes was about 45.3% (w/w), and the real specific activity close to 3.26 U mg⁻¹. The K_m values did not significantly change between free (12.8 g L⁻¹) and immobilized enzymes (14.2 g L⁻¹), due to the absence of diffusional limitation. The IMER system presented more than 80% of its residual activity after 5000 column volumes, highlighting the high stability of the immobilized endodextranases. Response surface methodology was used to enhance the performance of the IMER. Depending on dextran concentrations and flow rates, specific patterns of IMOs distributions were observed during the enzymatic hydrolysis. Finally, prebiotic activity was also investigated on IMOs produced by medium conditions (flow rate 0.3 mL min⁻¹ and dextran concentrations 4% w/w) against Lactobacillus rhamnosus GG (ATCC 53103). Their scores were at least as good as two commercialized fructo-oligosaccharides (FOS), Fibrulose^® F97 and Orafti^® P95.     

Protocorm culture of Dendrobium candidum in balloon type bubble bioreactors

Protocorm cultures of Dendrobium candidum were established in balloon type bubble bioreactors using Murashige and Skoog (MS) medium with 0.5 mg l⁻¹ α-naphthaleneacetic acid (NAA), 2.5% (w/v) sucrose, 5:25 mM NH₄:NO₃ and 1% (v/v) banana homogenate for the production of biomass and bioactive compounds. In 3 l bioreactor containing 2 l medium, a maximum protocorm biomass (21.0 g l⁻¹ dry biomass) and also optimum quantities of total polysaccharides (389.3 mg g⁻¹ DW), coumarins (18.0 mg g⁻¹ DW), polyphenolics (11.9 mg g⁻¹ DW), and flavonoids (4.5 mg g⁻¹ DW) were achieved after 7 weeks of culture. Based on these studies, 5 and 10 l bioreactor cultures were established to harvest 80 g and 160 g dry biomass. In 10 l bioreactors, the protocorms grown were accumulated with optimal levels of polysaccharides (424.1 mg g⁻¹ DW), coumarins (15.8 mg g⁻¹ DW), polyphenols (9.03 mg g⁻¹ DW) and flavonoids (4.7 mg g⁻¹ DW). The bioreactor technology developed here will be useful for the production of important bioactive compounds from D. candidum.     

Effect of soybean oil and Tween 80 on the production of botryosphaeran by Botryosphaeria rhodina MAMB-05

The addition of soybean oil and Tween 80 was evaluated with the objective of increasing the production of botryosphaeran, an exopolysaccharide (EPS) of the (1 → 3;1 → 6)-β-d-glucan type produced by the fungus Botryosphaeria rhodina MAMB-05. Factorial design and analysis by response surface methodology was developed to select the main factors that would affect and enhance EPS production. The optimized culture conditions were: 40 g l⁻¹ glucose with 10 ml l⁻¹ soybean oil, and 4.5 ml l⁻¹ Tween 80, during 72 h cultivation at 28 °C (180 rpm) and initial pH 5.7. The predicted result for botryosphaeran production was 8.22 ± 1.36 g l⁻¹, and compared with the experimental value of 7.74 ± 0.13 g l⁻¹. Partial characterization of the botryosphaeran produced under the optimized conditions showed one type of polysaccharide with β-glycosidic linkages containing glucose as monosaccharide.