Estudio comparativo de la producción de biomasa en fermentación superficial y en estado líquido de macromicetos con diferentes fuentes nutrimentales / Comparative study of the production of biomass in surface fermentation and in the liquid state of macromycetes with different nutrient sources

RESUMEN Los macromicetos han adquirido gran interés por su importancia alimenticia, terapéutica y económica, razón por la cual es necesario enfocar esfuerzos en la búsqueda de optimizar su producción de biomasa. El presente trabajo buscó determinar y comparar el efecto de la fermentación líquida (FEL) y superficial (FeSup) (medio solido) sobre la producción de biomasa de Flammulina velutipes, Hypsizigus tessulatus y Grifola frondosa empleando seis fuentes de nutrientes de bajo costo: harina de soja, trigo integral, maíz blanco, maíz amarillo precocido, salvado de trigo y semillas de linaza molida. Los resultados de la FeSup permitieron determinar que la especie de mayor crecimiento radial, indistintamente de la fuente de nutrientes, es F. velutipes seguida de H. tessulatus y por ultimo G. frondosa. Adicionalmente, la mayor producción de biomasa con FeSup se observa para F. velutipes y H. tessulatus (6,4480 g/L y 5,7320 g/L, respectivamente) Por el contrario, para la FEL, G. frondosa (11,4620 g/L) es la especie de mayor producción. La comparación en la producción de biomasa empleando FEL y FeSup, evidenció que los resultados son dependientes de la técnica de cultivo y que la FeSup no puede ser empleada para la selección preliminar de hongos macromicetos, enfocada en la producción de biomasa por FEL.

ABSTRACT Macromycetes have acquired great interest because of their nutritional, therapeutic and economic importance, which is why it is necessary to focus efforts in the search to optimize their biomass production. The present work sought to determine and compare the effect of liquid fermentation (FEL) and surface fermentation (FeSup) (solid medium) on the biomass production of Flammulina velutipes, Hypsizigus tessulatus and Grifola frondosa using six sources of low cost nutrients: soybeans, whole wheat, white corn, precooked yellow corn, wheat bran and ground flax seed. The results of the FeSup allowed to determine that the species with the highest radial growth, indistinctly from the nutrient source, is F. velutipes followed by H. tessulatus and finally G. frondosa. Additionally, the highest biomass production with FeSup is observed for F. velutipes and H. tessulatus (6.4480 g/L and 5.7320 g/L, respectively) On the contrary, for the FEL, G. frondosa (11.4620 g/L) is the species with the highest production. The comparison in the production of biomass using FEL and FeSup, showed that the results are dependent on the culture technique and that the FeSup cannot be used for the preliminary selection of fungi macromycetes, focused on the production of biomass by FEL.

Producción de unidades infectivas de Isaria fumosorosea (Hypocreales: Cordycipitaceae) a partir de aislados nativos del noreste de México mediante 3 estrategias de propagación / Production of infectious units of Isaria fumosorosea ( Hypocreales: Cordycipitaceae) from different indigenous isolates of northeastern Mexico using 3 propagation strategies

El objetivo del presente estudio fue evaluar la producción de blastosporas y conidios de diferentes aislados nativos de México del hongo entomopatógeno Isaria fumosorosea y de una cepa de colección mediante diferentes técnicas de propagación. En la producción de blastosporas se utilizaron 2 medios de cultivo líquidos (sumergidos), uno a base de casaminoácidos y el otro a base de peptona de colágeno como fuentes de nitrógeno, con glucosa como fuente de carbono en ambos. Para la producción de conidios, los hongos se cultivaron en agar papa dextrosa, a partir de esos cultivos se prepararon suspensiones de 1 x 10(6) conidios/ml para inocular matraces con caldo dextrosa Sabouraud, para iniciar así la fase líquida del cultivo bifásico, denominado también precultivo. Posteriormente con el precultivo y las suspensiones de conidios se inocularon bolsas con granos de arroz, que se incubaron durante 14 días para el cultivo bifásico y para la fermentación sólida, respectivamente. El aislado HIB-23 fue el que logró la más elevada concentración de blastosporas obtenida en el cultivo sumergido: 4,90 x 10(8) blastosporas/ml en el medio casaminoácidos; y en el medio con peptona de colágeno se obtuvieron 2,15 x 10(8) blastosporas/ml. La máxima producción de conidios en fermentación sólida la logró la cepa Pfr-612 (1,58 x 10(9) conidios/g), mientras que la máxima en cultivo bifásico correspondió al aislado HIB-30 (9,00 x 10(6) conidios/g). La fermentación sólida resultó ser el método más efectivo, con un promedio de 1,09 x 10(9) conidios/g, mientras que el cultivo bifásico fue el menos efectivo, con un promedio de 2,76 x 10(6) conidios/g. Para la producción de blastosporas en los medios sumergidos no se obtuvo diferencia significativa alguna.

The aim of this study was to evaluate the production of blastospores and conidia of different native isolates and a strain of Isaria fumosorosea using different propagation techniques. Two liquid culture media of casamino acids and peptone as nitrogen sources and glucose as carbon source for both media cultures were respectively used in the production of blastospores, while for the production of conidia, the fungi were grown in potato dextrose agar; from these cultures, solutions of conidia to a concentration of 1 x 10(6) per milliliter were prepared to inoculate flasks with Sabouraud dextrose broth for the liquid phase of the biphasic culture, also known as preculture. Subsequently, rice grain bags were inoculated with the preculture and the conidia solutions, which were incubated for 14 days for solid fermentation and biphasic culture, respectively. The HIB-23 isolate recorded a concentration of 4.90 x 10(8) blastospores/ml in the casamino acid medium, while a concentration of 2.15 x 10(8) blastospores/ml was obtained in the peptone collagen medium. For the Pfr-612 strain, the conidia production in solid-state fermentation was 1.58 x 10(9) conidia/g, and for HIB-30 in the biphasic culture of 9.00 x 10(6) conidia/g. Solid-state fermentation proved to be the most effective method with an average of 1.09 x 10(9) conidia/g, whereas the biphasic culture was the least effective method with 2.76 x 10(6) conidia/g; no significant difference was reported for the submerged production media.

Optimization of submerged culture for biomass and polysaccaharide of Pleurotus ostreatus BPPTCC 6017 using response surface methodology

Aims: Polysaccharide of Pleurotus ostreatus is one of the fungal polysaccharide which has been widely studied, produced by extracting the fruiting body. An alternative method for producing polysaccharide of P. ostreatus directly from the mycelia instead of the fruiting body is through submerged culture. This study was aimed to determine the optimum submerged culture conditions for producing biomass and intracellular polysaccharide of the oyster mushroom. Methodology and results: P. ostreatus BPPTCC 6017 was collected from traditional mushroom farm in West Java, Indonesia. Submerged fermentation was conducted in 1000 mL medium (2 L flask). Four variables were tested: temperature, pH, agitation, and fermentation time, using central composite design of the response surface methodology. Mycelial biomass produced, was extracted to obtain water-soluble and alkali-soluble polysaccharide. Experimental data obtained were fitted to a second-order polynomial equation using multiple regression analysis and also analysed by appropriate statistical methods. The 3-D response surface plots derived from the mathematical models were applied to determine the optimum conditions: temperature 27.89 °C, initial pH medium 5.49, agitation 124.08 rpm, and fermentation time 11.44 days. The predicted results of the models were 33.75 g/L mycelia, 0.33 g/L water-soluble polysaccharide, and 0.64 g/L alkali-soluble polysaccharide. Those results were then verified on the optimum conditions, and produced 32.00±1.25 g/L mycelia, 0.29±0.01 g/L water-soluble polysaccharide and 0.60±0.02 g/L alkali-soluble polysaccharide, were close to the theoretical predictions. Conclusion, significance and impact study: The present study was a first effort to assess and obtain the optimum conditions for producing the biomass and polysaccharides of the strain P. ostreatus BPPTCC 6017 using submerged fermentation

Screening of wild type Streptomyces isolates able to overproduce clavulanic acid

The selection of new microorganisms able to produce antimicrobial compounds is hoped for to reduce their production costs and the side effects caused by synthetic drugs. Clavulanic acid is a β-lactam antibiotic produced by submerged culture, which is widely used in medicine as a powerful inhibitor of β-lactamases, enzymes produced by bacteria resistant to antibiotics such penicillin and cephalosporin. The purpose of this work was to select the best clavulanic acid producer among strains of Streptomyces belonging to the Microorganism Collection of the Department of Antibiotics of the Federal University of Pernambuco (DAUFPE). Initially, the strains were studied for their capacity to inhibit the action of β-lactamases produced by Klebsiella aerogenes ATCC 15380. From these results, five strains were selected to investigate the batch kinetics of growth and clavulanic acid production in submerged culture carried out in flasks. The results were compared with the ones obtained by Streptomyces clavuligerus ATCC 27064 selected as a control strain. The best clavulanic acid producer was Streptomyces DAUFPE 3060, molecularly identified as Streptomyces variabilis, which increased the clavulanic acid production by 28% compared to the control strain. This work contributes to the enlargement of knowledge on new Streptomyces wild strains able to produce clavulanic acid by submerged culture.

Improvement of submerged culture conditions to produce colorants by Penicillium purpurogenum

Safety issues related to the employment of synthetic colorants in different industrial segments have increased the interest in the production of colorants from natural sources, such as microorganisms. Improved cultivation technologies have allowed the use of microorganisms as an alternative source of natural colorants. The objective of this work was to evaluate the influence of some factors on natural colorants production by a recently isolated from Amazon Forest, Penicillium purpurogenum DPUA 1275 employing statistical tools. To this purpose the following variables: orbital stirring speed, pH, temperature, sucrose and yeast extract concentrations and incubation time were studied through two fractional factorial, one full factorial and a central composite factorial designs. The regression analysis pointed out that sucrose and yeast extract concentrations were the variables that influenced more in colorants production. Under the best conditions (yeast extract concentration around 10 g/L and sucrose concentration of 50 g/L) an increase of 10, 33 and 23% respectively to yellow, orange and red colorants absorbance was achieved. These results show that P. purpurogenum is an alternative colorants producer and the production of these biocompounds can be improved employing statistical tool.

Produção e extração de colorantes naturais de Penicillium purpurogenum DPUA 1275 / Production and extraction of natural colorants from Penicillium purpurogenum DPUA 1275

Há interesse mundial no desenvolvimento de pesquisas envolvendo produção e extração de colorantes naturais, devido a sérios problemas de segurança industrial associados ao uso de colorantes sintéticos. Este trabalho objetivou produzir colorantes naturais de Penicillium purpurogenum DPUA 1275 por cultivo submerso (em frascos agitados e em biorreator) e estudar a extração dos colorantes vermelhos. Para a produção, os estudos iniciais mostraram que 5 discos de micélio, sacarose e extrato de levedura como fontes de carbono e nitrogênio, respectivamente, e 336 horas de cultivo eram condições adequadas para a produção dos colorantes. Visando à otimização da produção, realizaram-se planejamentos fatoriais, com as variáveis independentes: tempo de cultivo; velocidade de agitação; pH; temperatura; concentração de sacarose e de extrato de levedura. As variáveis-respostas foram produção de colorantes amarelos, laranjas e vermelhos. Dos resultados obtidos, as variáveis mais significativas ao processo foram concentrações de extrato de levedura e de sacarose. A produção dos colorantes vermelhos foi otimizada, alcançando a produção de 2,97 UA490nm, nas condições 48,90 e 11,80 g/L de sacarose e extrato de levedura, respectivamente, 30°C, pH 4,5 150 rpm e 336 horas de cultivo. Nos experimentos em biorreator, o melhor resultado foi obtido na frequência de agitação de 500 rpm e na mudança do pH do meio para 8,0, após 96 horas de bioprocesso. Ademais, avaliou-se a estabilidade dos colorantes vermelhos presentes no meio fermentado em diferentes condições (pH, temperatura, sais, polímeros e tensoativos). Referente a pH e temperatura, os colorantes vermelhos mostraram-se mais estáveis nas condições alcalinas e a 70 °C. Tanto os sais (NaCl e Na2SO4) quanto os polímeros (PEG 1.000, 6.000 e 10.000 g/mol e NaPA 8.000 g/mol a 5 e 15%) e os tensoativos (Tween 20, CTAB e SDS) não causaram perda da cor nas condições avaliadas. Estudos de solubilidade e de coeficiente de partição octanol-água mostraram que os colorantes vermelhos apresentam solubilidade superior em solventes polares e característica mais hidrofílica. Nos estudos de extração, as técnicas avaliadas foram Sistemas Poliméricos de Duas Fases Aquosas (SPDFA) formados pelo sistema PEG/NaPA e Colloidal Gas Aphrons (CGA). Pela primeira técnica, os colorantes vermelhos migraram preferencialmente para a fase PEG. Os polímeros PEG 6.000 g/mol, na presença de NaCl 0,1 e 0,5 M, e PEG 10.000 g/mol, com Na2SO4 0,5M, se destacaram dentre as condições analisadas com coeficiente de partição (K) próximo a 13, em ambos os casos, e seletividade de proteínas (SeP) próximas a 3. Para a técnica de CGA, o CTAB proporcionou os melhores resultados, seguido do Tween 20. Porém, o valor de K foi inferior ao obtido com SPDFA, com um máximo de 5 (CTAB 2 mM/pH 9,0). Os resultados obtidos demonstram um novo produtor de colorantes naturais, as quais têm potencial de aplicação em diversos segmentos industriais. Ademais, os resultados obtidos mostraram a eficiência das técnicas utilizadas para extração dos colorantes vermelhos, com destaque para SPDFA, que apresentou maiores valores de K

There is worldwide interest in developing research projects involving the production and extraction of natural colorants due to serious safety problems associated with industrial use of synthetic ones. The aim of this work was to investigate the production of natural colorants from Penicillium purpurogenum DPUA 1275 by submerged culture (rotatory shaker and bioreactor) besides studying the red colorants extraction. To the production step, initial studies showed that 5 agar mycelial discs, sucrose and yeast extract as carbon and nitrogen sources, respectively, and 336 hours of bioprocess promoted the best results. To optimize the colorants production a serie of factorial designs were performed. The independent variables studied were: fermentation time, agitation speed, pH, temperature, sucrose and yeast extract concentration under the responses production of yellow, orange and red colorants. From these results, the most significant variables for the process were sucrose and yeast extract concentration. The red colorants production was optimized achieving 2.97 UA490nm, in the following conditions: 48.90 and 11.80 g/L of sucrose and yeast extract, respectively, 30 °C, 4.5 pH, 150 rev min-1 and 336 hours of culture. In the experiments performed in bioreactor, the condition that promoted the best results was 500 rpm and pH adjusted for 8.0 after 96 hours of bioprocess. Furthermore, we evaluated the red colorants stability at different conditions (pH, temperature, salts, polymers and surfactants). Concerning to pH and temperature, the red colorants were more stable under basic conditions and 70 °C; not only the salts (NaCl and Na2SO4) but also the polymers (PEG 1000, 6000 and 10000 g/mol and NaPA 8000 g/mol) and the surfactants (Tween 20, CTAB and SDS) not promoted loss of color upon the conditions evaluated. Studies of red colorants solubility and octanol water coefficient showed that these compounds exhibit a higher solubility in polar solvents and present hydrophilic characteristics. Subsequently, the extraction of red colorant was evaluated through two extraction methods: Polymeric Systems Aqueous Two Phase (ATPS) composed by PEG and NaPA and Colloidal Gas Aphrons (CGA). For the first technique, the red colorant preferentially migrated to the PEG phase. The best results were obtained with PEG 6000 g/mol in the presence of 0.1 to 0.5 M NaCl and with PEG 10000 g/mol with 0.5 M Na2SO4. To both cases the partition coefficient (K) was close to 13 and the Selectivity in terms of proteins (SeP) was close to 3. For the CGA technique, CTAB gave the best results followed by Tween 20. However, the K values were lower than the ones obtained with ATPS with a maximum of 5 in the following condition: CTAB 2 mM/pH 9.0. For the SeP, the values obtained for both techniques were close. The results above show a new producer of natural colorants which have potential application in various industries. Moreover, the results show the efficiency of the techniques used to extract the red colorants, especially to ATPS that presented higher K values

Optimization of exopolysaccharides production from a novel strain of Ganoderma lucidum CAU5501 in submerged culture

This study aimed at optimizing the medium of a new Ganoderma lucidum strain CAU5501 to enhance the yield of exopolysaccharides (EPS) and mycelial growth. Firstly, the suitable level of glucose, magnesium, phosphate and C/N ratio was determined by single factor experiment. Subsequently, the optimum concentrations of these medium components were investigated using the orthogonal matrix method. The results indicated that the higher levels of EPS were correlated with the level of cell growth when glucose concentration was studied (data no show). The optimum medium for EPS yield was found to be 70 g/l glucose, 5 C/N ratio, 2.5 g/l KH2PO4, 0.75 g/l MgSO4·7H2O, and for mycelial growth was 50 g/l glucose, 5 C/N ratio, 1.5 g/l KH2PO4, 0.5 g/l MgSO4·7H2O. When cultivated in the obtained optimal media in 3 L shake flask, compared to the basal medium, the EPS yield increased markedly from 1.003 to 1.723 g/l, and the mycelium formation was also markedly improved from 2.028 to 7.235 g/l. Results obtained in this study are beneficial to further study for enhancing the production of Ganoderma lucidum polysaccharides in large scale commercialized production.

Antioxidant activity of the extracts from Pycnoporus sanguineus mycelium

The aim of this work was to study the production of compounds with antioxidant activity by Pycnoporus sanguineus when cultivated in submerged fermentation using a potato dextrose broth plus peptone medium. The study evaluated the biomass production, glucose consumption, variation of medium pH and antioxidant activity. The antioxidant potential was tested through the DPPH method and β-carotene / linoleic acid system with extracts obtained from the mycelium at different times of cultivation (5, 10, 15, 20, 25 and 30 days). Maximum kinetic values of specific growth rate (0.289 day-1), biomass productivity (0.698 g.L-1.day-1) and the yield of glucose conversion into biomass (26.24 g.g-1) were obtained during the exponential growth phase. The highest antioxidant activity was registered during the stationary phase, with a similar potential as the synthetic antioxidant BHT, in the extracts obtained at 30 days of cultivation.

Influencia de la concentración de inóculo en la producción de celulasa y xilanasa por aspergillus niger / Influence of inoculum concentration on the cellulase and xylanase production by aspergillus niger

Existe un gran interés por el uso de enzimas lignocelulolíticas en varias industrias, y en la biodegradación de biomasa para la producción de biocombustibles y otras aplicaciones. Entre las fuentes microbianas de enzimas, Aspergillus niger es uno de los microorganismos más utilizados en la producción de enzimas industriales, debido a sus niveles altos de secreción de proteína y a su condición GRAS (generally regarded as safe). El objetivo del presente estudio fue evaluar la influencia de la concentración de inóculo en la morfología y producción de celulasas y xilanasas con A. niger en cultivo sumergido. Para ello, fueron inoculados matraces de 250 mL con 40 mL de medio con 3% (v/v) de una suspensión de 104 o 108 esporas por mililitro e incubados a 28 ºC y 175 rpm durante 120 horas. Se utilizaron 10 g*L-1 de lactosa como fuente de carbono. En cada caso se determinó la cantidad de biomasa, la proteína extracelular soluble, lactosa residual, actividad celulasa total y xilanasa cada 24 horas. Aunque no hubo un efecto notorio en la morfología de crecimiento, salvo en el color y el diámetro de pellets obtenidos, sí se afectó la µmax (0,06 y 0,03 h-1 para 104 y 108 esporas*mL-1, respectivamente) y la concentración máxima de biomasa. Además, mientras que las productividades volumétricas de celulasa (ΓFPA) (8,2 y 8,0 UI.*L-1*h-1 para 104 y 108 esporas*mL-1, respectivamente) fueron similares para ambos inóculos, la productividad de xilanasa (ΓXIL) fue mayor para el inóculo más concentrado (29,7 y 33,4 UI¨*L-1*h-1 para 104 y 108 esporas*mL-1, respectivamente). Los resultados indican que la productividad de celulasas y xilanasas está estrechamente relacionada con la concentración de inóculo.

There is a great interest for the use of lignocellulolytic enzymes in several industries and in biomass degradation for production of biofuels and other applications. Among the microbial sources of enzymes, Aspergillus niger is one of the most used microorganisms in the production of industrial enzymes due to its high levels of protein secretion and its GRAS (generally regarded as safe) condition. The aim of the present study was to evaluate the influence of A. niger inoculum concentration in the morphology and production of cellulases and xylanases in submerged cultures. For this, 250 mL flasks containing 40 mL culture medium were inoculated with a 3% (v/v) of either 104 or 108 spores per milliliter suspension and incubated at 28 º C and 175 rpm during 120 hours. Lactose (10 g*L-1) was used as the carbon source. In each case, the amount of biomass, the extracellular soluble protein, residual lactose, total celullase activity and xylanase activity were determined every 24 hours. Even thought there was not a notorious effect on the growth morphology, except in color and diameter of pellets; µmax was affected (0.06 and 0.03 h-1 for 104 and 108 spores*mL-1, respectively) as well as maximum biomass concentration. In addition, while the volumetric productivity of cellulase (8.2 and 8.0 UI*L-1*h-1 for 104 and 108 spores*mL-1, respectively) were similar for both inocula, the productivity of xylanase was greater for the more concentrated inoculum (29.7 and 33.4 UI*L-1*h-1 for 104 and 108 spores*mL-1, respectively).The results show that cellulase and xylanase productivities are closely related to the inoculum concentration.

Optimal Culture Conditions for Mycelial Growth and Exo-polymer Production of Ganoderma applanatum

The effect of fermentation parameters and medium composition on the simultaneous mycelial growth and exo-polymer production from submerged cultures of Ganoderma applanatum was investigated in shake-flask cultures. The optimum initial pH for mycelial growth and exo-polymer production was 5.0 and 6.0, respectively. The optimum temperature was 25degrees C and the optimum inoculum content was 3.0% (v/v). The optimal carbon and nitrogen sources were glucose and corn steep powder, respectively. After 12 days fermentation under these conditions, the highest mycelial growth was 18.0 g/l and the highest exo-polymer production was 3.9 g/l.

Availability of Sikhae Factory Wastewater as a Submerged Culture Medium for Lentinula edodes

Sikhae is a Korean traditional beverage of saccharified rice. Its factory waste (SFW) is usually thrown away instead of being used. We developed a cheap substrate of SFW for use in liquid spawn that is known for its higher fruit body yields than grain spawn in sawdust cultivation. Mycelia of Lentinula edodes ASI 3046, which is regarded as the most suitable strain for sawdust cultivation, were cultured on six kinds of previous known media and SFW. As the seven kinds of media were applied, a Sikhae Factory Waste (SFW) was most excellent in growth. The dried mycelial weight in SFW was almost four times as much as that in the other media. In the flask culture, optimum culture conditions for the mycelial growth were obtained after 13 days of cultivation at media volume of 100 ml, 100 rpm, initial pH 4.5, and 25degrees C. The best mycelial growth was observed when MgSO4 . 7H2O and D-sucrose were added as a supplement in SFW. SWM must be a remarkable medium for L. edodes because of its simple preparation and low cost.

STUDIES ON THE SUBMERGED-CULTURE TECHNOLOGY FOR COPRINUS COMATUS FR. CC-8810 / 微生物学通报

Suitable conditions for polysaccharide production in submerged culture by Coprinus comatus Ft. CC-8810 were: glucose 40g, Soybean cake powder 30g, yeast extract powder 5.0g, bran 30g, KH_2PO_4 1.0g, MgSO_4?7H_2O 0.5g, tap water 1L, pH5—6, 28℃, 160r/min. Seed culture grown in shake flask for 4 days were inoculated into 1.5L fermentor. After 5—6 days the fermentation ended up with decreases in pH to 4.9—5.0 and in reducing sugar to 1.2%. 45.1g(dry Wt.)/L hyphae and 3.6g/L polysaccharide were obtained.

Characterization of Aminoacylase in the Mycelial Cell of Cunnighamella echinulata / 微生物学通报

The strain of Cunninghamella echinulata 9980 was first selected with high aminoacylase activity . In three submerged cultures, the aminoacylase activity in the mycelial cell was compared . A number of factors have effects on the resolution reaction. The results showed that, peptone culture gave the highest aminoacylase activity with 680U/g.The optium temperature,pH,and substrate concentration were 55℃, 7.0,and 0.2mol/L,respectively. The ions in the buffer lowered the activity,but the Co~(2+) in 10~(-4)~10~(-3 )mol/L was necessary for its activity.