Effect of shear stress on anthraquinones production by Rubia tinctorum suspension cultures

Suspension cultures of Rubia tinctorum, an anthraquinones (AQs) producer, were grown both in Erlenmeyer flasks at 100 rpm and in a 1.5 L mechanically stirred tank bioreactor operating at 450 rpm. The effect of hydrodynamic stress on cell viability, biomass, and AQs production was evaluated. Cell viability showed a transient decrease in the bioreactor during the first days, returning to the initial values toward the end of the culture time. The biomass obtained in the bioreactor was 29% lower than that attained in the Erlenmeyer flasks. The H2O2 production in the bioreactor (with peaks at 7 and 10 days) was about 15 times higher than that obtained in the flasks. A clear relationship exists between the maximum concentration of H2O2 generated and AQs produced. The AQs content in the bioreactor was 233% higher than that in the Erlenmeyer flasks. The AQs specific productivity in the stirred tank and in the Erlenmeyer flasks was 70.7 and 28.5 micromol/g FW/day, respectively. This production capability was maintained in the regrowth assays. On the other hand, the negative effects of hydrodynamic stress on viability and biomass concentration observed in the bioreactor culture were reverted in the regrowth cultures. It can be concluded that R. tinctorum suspension cultures are able to grow in stirred tanks at 450 rpm responding to the hydrodynamic stress with higher concentrations of AQs, which suggest the possibility of a technological approach taking advantage of this phenomenon.     

Conidiation ofTrichoderma atroviride isolate during submerged cultivation in a laboratory stirred-tank fermenter

Conditions for conidiation of a natural isolate of Trichoderma atroviride during submerged cultivation in Erlenmeyer flasks and in a laboratory stirred-tank fermenter were optimized. From the simple sugars tested, cellobiose was the best substrate for conidia production while cellulose fines from paper mill waste proved to be a suitable cheap complex carbon source. Optimum temperature for conidiation was 24-26 degrees C, and the required dissolved oxygen level was > 40% saturation. After initial slight decrease during the 1st d after inoculation, the pH of the culture medium constantly increased throughout the sporulation period. Attempts to regulate the pH during fermentation did not improve the spore yields. The most intense formation of conidia took place between 2nd and 3rd d of growth and the overall volumetric productivity of conidia was 4.1-8.2 x 10(9) conidia per L/h.     

Cellulase On-Site Production from Sugar Cane Bagasse Using Penicillium echinulatum

Penicillium echinulatum was evaluated as a cellulolytic enzyme producer in shaking flasks and bioreactor submerged culture using sugarcane bagasse as carbon source. Sodium hydroxide delignified steam-exploded pretreated bagasse (SDB) and hydrothermal pretreated bagasse had a maximum filter paper activity (FPase) of 2.4 and 2.6 FPU/mL, respectively. Delignified acid pretreated bagasse and Celufloc 200TM (CE) carbon sources displayed maximum FPase of 1.3 and 1.6 FPU/mL while in natura bagasse (INB) provided the lowest enzyme activity, ca. 0.4 FPU/mL. Measurement of surface specific area of lignocellulosic material and scanning electron microscopic images showed a possible correlation between fungal mycelia accessibility to lignocellulosic particles and obtained cellulolytic enzyme activity of fermentation broth. Fed-batch experiments performed in a controlled bioreactor attained the highest value of FPase of 3.7 FPU/mL, enzyme productivity of 25.7 FPU/L h, and enzyme yield from cellulose equal to 134 FPU/g with SDB. Enzyme hydrolysis of steam-pretreated bagasse accomplished with the obtained supernatant of fermentation broth (10 FPU/g of biomass and 5 % w/v) performed better than commercial cellulose complex. The results showed that P. echinulatum has potential to be used as an on-site enzyme platform aiming second bioethanol production from sugarcane lignocellulosic residue.     

A simple eccentric stirred tank mini‐bioreactor: Mixing characterization and mammalian cell culture experiments

In industrial practice, stirred tank bioreactors are the most common mammalian cell culture platform. However, research and screening protocols at the laboratory scale (i.e., 5–100 mL) rely primarily on Petri dishes, culture bottles, or Erlenmeyer flasks. There is a clear need for simple—easy to assemble, easy to use, easy to clean—cell culture mini‐bioreactors for lab‐scale and/or screening applications. Here, we study the mixing performance and culture adequacy of a 30 mL eccentric stirred tank mini‐bioreactor. A detailed mixing characterization of the proposed bioreactor is presented. Laser induced fluorescence (LIF) experiments and computational fluid dynamics (CFD) computations are used to identify the operational conditions required for adequate mixing. Mammalian cell culture experiments were conducted with two different cell models. The specific growth rate and the maximum cell density of Chinese hamster ovary (CHO) cell cultures grown in the mini‐bioreactor were comparable to those observed for 6‐well culture plates, Erlenmeyer flasks, and 1 L fully instrumented bioreactors. Human hematopoietic stem cells were successfully expanded tenfold in suspension conditions using the eccentric mini‐bioreactor system. Our results demonstrate good mixing performance and suggest the practicality and adequacy of the proposed mini‐bioreactor. Biotechnol. Bioeng. 2013; 110: 1106–1118. © 2012 Wiley Periodicals, Inc.     

Production of Choristoneura fumiferana Nucleopolyhedrovirus in C. fumiferana (CF-2C1 Cells) in a 3 Litre Bioreactor Using Serum-free Medium

The purpose of this study was to develop a cell culture process in a bioreactor for the production of a viral insecticide for the spruce budworm, Choristoneura fumiferana . Several cell lines were tested for their growth in serum-free medium suspension cultures. One cell line, CF-124T-2C1 (CF-2C1), was successfully adapted to grow in suspension cultures in SFM. Serum-free Ex-Cell 405 medium produced a much higher cell density (6.3 x 10 6 cells ml -1 ) than the Grace's medium supplemented with 10% fetal bovine serum (2.5 x 10 6 cells ml -1 ). Also, a higher yield of virus was obtained in the former medium. Ex-Cell 405, was used to study the growth of CF-2C1 cells and the production of C. fumiferana nucleopolyhedrovirus (CfMNPV) in a 3 l bioreactor. Under these conditions, a specific growth rate ( μ) of 0.027 h -1 was obtained during the exponential growth phase, and the specific carbon dioxide evolution rate, as determined by on-line measurement, was 0.9 x 10 -16 mol cell -1 s -1 and 1.78 x 10 -16 mol cell -1 s -1 during growth and infection phases, respectively. Virus production in bioreactor cultures infected at 1.3 x 10 6 cells ml -1 was consistently lower than that obtained in Erlenmeyer shake flasks. Only 26% of the cells were infected in the bioreactor compared to 44% in the shake flasks. However, a higher yield of occluded virus was obtained in the bioreactor cultures than in shake flasks. The production of occlusion bodies (OB) achieved in bioreactor cultures was 2 x 10 6 OB ml -1 .     

Evaluation of inert and organic carriers for <Emphasis Type="Italic">Verticillium lecanii</Emphasis> spore production in solid-state fermentation

Growth and sporulation of Verticillium lecanii on inert and organic carriers (sugar-cane bagasse, corncob, rice straw, polyurethane foam and activated carbon) in a solid-state fermentation process was studied. Sugar-cane bagasse and polyurethane foam produced 10¹⁰ spores g⁻¹ dry carrier whereas corncob, rice straw, and activated carbon yielded, respectively 8 × 10⁹, 4 × 10⁹, and 3 × 10⁸ spores g⁻¹. Chitinase activity of the conidia was in the following order: sugar-cane bagasse (3.3 U mg⁻¹) > wheat bran (3.0 U mg⁻¹) > polyurethane foam (2.7 U mg⁻¹). There was no significant difference (2.5–2.7 U mg⁻¹) in the proteinase activity among the conidia from the three cultures. Scanning electron microscopy shows that aerial mycelium freely penetrated into the internal area of polyurethane foam. Sugar-cane bagasse provided enough area for vegetative hyphae to attach. Of the carriers analyzed, polyurethane foams and sugar-cane bagasse were the best carriers for V. lecanii growth and spore production.     

Fermentation of cellulosic hydrolysates obtained by enzymatic saccharification of sugarcane bagasse pretreated by hydrothermal processing

This work aims to evaluate the fermentability of cellulosic hydrolysates obtained by enzymatic saccharification of sugarcane bagasse pretreated by hydrothermal processing using Candida guilliermondii FTI 20037 yeast. The inoculum was obtained from yeast culture in a medium containing glucose as a carbon source supplemented with rice bran extract, CaCl₂·2H₂O and (NH₄)₂SO₄ in 50 mL Erlenmeyer flasks, containing 20 mL of medium, initial 5.5 pH under agitation of an orbital shaker (200 rpm) at 30°C for 24 h. The cellulosic hydrolysates, prior to being used as a fermentation medium, were autoclaved for 15 min at 0.5 atm and supplemented with the same nutrients employed for the inoculum, except the glucose, using the same conditions for the inoculum, but with a period of 48 h. Preliminary results showed the highest consumption of glucose (97%) for all the hydrolysates, at 28 h of fermentation. The highest concentration of ethanol (20.5 g/L) was found in the procedure of sugarcane bagasse pretreated by hydrothermal processing (195°C/10 min in 20 L reactor) and delignificated with NaOH 1.0% (w/v), 100°C, 1 h in 500 mL stainless steel ampoules immersed in an oil bath.     

Relation between Citric Acid Production and Respiration Rate of Aspergillus niger in Solid‐State Fermentation

Among the organic acids produced industrially, citric acid is the most important in quantitative terms. Solid‐state fermentation (SSF) has been an alternative method for citric acid production using agro‐industrial residues such as cassava bagasse (CB). The use of CB as a substrate can avoid environmental problems caused by its disposal into the environment. This study was developed to verify the influence of the treated bagasse amount, and consequently, the influence of the gelatinization degree of CB starch on citric acid production by SSF in Erlenmeyer flasks, horizontal drums, and trays. The best results were obtained in a horizontal drum bioreactor using 100 % of treated CB. However, trays showed advantages and good perspectives for large‐scale citric acid production due to economic reasons such as energy costs. A kinetic study was also carried out in order to compare citric acid production in glass columns (laboratory scale) and horizontal drum bioreactors (semi‐pilot scale). This study was accomplished in order to follow the influence of aeration on citric acid accumulation. In addition, the production of CO₂ was evaluated as an indirect method of biomass estimation. Citric acid production was higher in glass columns (309.70 g/kg of dry CB) than in HD bioreactors (268.94 g/kg of dry CB). Finally, it was possible to show that citric acid production was favored by a limited biomass production, which occurred with low aeration rates. Biomass production is related to CO₂ production and as a result, a respirometry analysis could be used for biomass estimation.     

Infection of the Coffee Berry Borer Hypothenemus hampei (Coleoptera: Scolytidae) by Brazilian Isolates of the Entomopathogenic Fungi Beauveria bassiana and Metarhizium anisopliae (Deuteromycotina: Hyphomycetes)

The virulence of four fungal isolates (three Beauveria bassiana and one Metarhizium anisopliae ) against adult female coffee berry borers (CBB) was investigated. The most virulent isolate from initial bioassays, B. bassiana LPP1, with a LT 50 of 3.4 days, was further investigated by application to berries prior to infestation and to berries already infested with CBB. At the highest concentration applied to berries (1 ×10 7 conidia mL -1 ), CBB mortality was 83% (berries inoculated prior to infestation) and 62% (berries inoculated after infestation).     

Use of immobilized Candida cells on xylitol production from sugarcane bagasse

In this study we used the yeast Candida guilliermondii FTI 20037 immobilized by entrapment in Ca-alginate beads (2.5-3 mm diameter) for xylitol production from concentrated sugarcane bagasse hemicellulosic hydrolysate in a repeated batch system. The fermentation runs were carried out in 125- and 250-ml Erlenmeyer flasks placed in an orbital shaker at 30 degrees C and 200 rpm during 72 h, keeping constant the proportion between work volume and flask total volume. According to the results, cell viability was substantially high (98%) in all fermentative cycles. The values of parameters xylitol yield and volumetric productivity increased significantly with the reutilization of the immobilized biocatalysts. The highest values of xylitol final concentration (11.05 g/l), yield factor (0.47 g/g) and volumetric productivity (0.22 g/lh) were obtained in 250-ml Erlenmeyer flasks containing 80 ml of medium plus 20 ml of immobilized biocatalysts. The support used in this study (Ca-alginate) presented stability in the experimental conditions used. The results show that the use of immobilized cells is a promising approach for increasing the xylitol production rates.     

Conidia production by Isaria fumosorosea on solid substrates and its pathogenicity towards Bemisia tabaci

Large amounts of conidia must be recovered to use Isaria fumosorosea as a biological control agent. Aerial conidia are mass-produced in solid substrate culture. Conidia obtained from growth on different substrates must be similar in quantity and quality (viability, purity and virulence). In the present work, several solid substrates were evaluated: rice, sorghum, sugarcane, corncob, plantain and wheat (derived from the production of Trichogramma sp.) to find alternatives that are economical and available in different regions. The highest conidia production was obtained on rice, plantain and corncob substrates, which yielded 5.33 × 10⁹ conidia/g, 5.24 × 10⁹ conidia/g and 4.8 × 10⁹ conidia/g substrate, respectively. At concentrations of 1 × 10⁷ conidia/mL, the mortality rates obtained with conidia developed on rice, plantain and corncob substrates were 98%, 97% and 88%, respectively. The lethal concentration 50 (LC₅₀₎ values of conidia obtained from rice and plantain were 7.2 × 10⁴ conidia/mL and 5.1 × 10⁴ conidia/mL, respectively.     

Ethanol production by coupled saccharification and fermenation of sugar cane bagasse

Summary As initial studies showed that enzymatic saccharification of sugar cane bagasse in columns with recycling of eluate was slightly more efficient than in agitated flasks, ethanol production by fermentation of the eluates with fast-decanting yeast and recycling of the fermentate through the bagasse columns was studied. The alcohol yield from these coupled columns after 24 or 48 h was more than 10% more than that in a simultaneous saccharification and fermentation in agitated flasks at 40°.     

Susceptibility of Sitophilus zeamais (Motsch.) (Coleoptera: Curculionidae) and Prostephanus truncatus (Horn) (Coleoptera: Bostrichidae) to Entomopathogenic Fungi from Ethiopia

The efficacy of 13 isolates of entomopathogenic fungi belonging to Beauveria , Metarhizium or Paecilomyces spp. was assessed against Sitophilus zeamais (Coleoptera: Curculionidae) and Prostephanus truncatus (Coleoptera: Bostrichidae) using a total immersion bioassay technique in the laboratory. Fungi were applied at concentrations of 1 ×10 7 and 1 ×10 8 conidia mL -1 for P. truncatus and S. zeamais , respectively. All isolates tested were virulent to P. truncatus (98-100% mortality, and median survival time (MST) ranged from 2.85-4.05 days). Metarhizium anisopliae and B. bassiana were also virulent to S. zeamais (92-100% mortality, MST ranged from 3.58-6.28 days). The isolate of Paecilomyces sp. was found to be the least virulent against S. zeamais , causing only 26.32 ±4.29% mortality with MST of 10.38 ±0.29 days. P. truncatus proved more susceptible to the entomopathogenic fungi tested than S. zeamais . One M. anisopliae (PPRC-EE) and three B. bassiana isolates (PPRC-HH, PPRC-9609 and PPRC-9614) were selected for further study and dose-mortality relationships were assessed on S. zeamais . The tested concentrations ranged from 1 ×10 4 -1 ×10 7 conidia mL -1 . M. anisopliae (PPRC-EE) showed the lowest LC 50 (3.39 ×10 5 conidia mL -1 ) followed by B. bassiana PPRC-HH (2.04 ×10 6 conidia mL -1 ). PPRC-9609 and PPRC-9614 showed slight differences in LC 50 but not at LC 90 . The results revealed the higher potency of M. anisopliae as compared with the B. bassiana isolates tested. The study suggests that the use of entomopathogenic fungi may hold promise as an alternative method to control pests of stored-products in Ethiopia.     

CO2 accumulation in bioreactor suspension cultures of Cyclamen persicum Mill. and its effect on cell growth and regeneration of somatic embryos

CO₂ accumulation in different culture systems containing embryogenic cell suspension cultures of cyclamen (Cyclamen persicum Mill.) was analyzed. In bioreactors equipped with a bubble-free or a bubble aeration system, CO₂ mole fractions in the gas phase of more than 10% were determined whereas in Erlenmeyer flasks, CO₂ mole fractions were below 2%. CO₂ accumulation in bioreactors was severely growth inhibiting in comparison to the flasks. By removing CO₂ in the aeration gas of a bubble-free aerated bioreactor, cell growth comparable to that in flasks was achieved. The regeneration ability of cell suspensions after being cultured in bioreactors with CO₂ accumulation was better than those after culture in bioreactors without CO₂ accumulation or in flasks. Received: 16 June 1998 / Revision received: 13 August 1998 / Accepted: 1 December 1998     

Physiological and antioxidant response by Beauveria bassiana Bals (Vuill.) to different oxygen concentrations

The effect of three levels of oxygen (normal atmosphere (21% O₂), low oxygen (16% O₂) and enriched oxygen (26% O₂)) on the production and germination of conidia by Beauveria bassiana was evaluated using rice as a substrate. The maximum yield of conidia was achieved under hypoxia (16% O₂) after 8 days of culture (1.51 × 10⁹ conidia per gram of initial dry substrate), representing an increase of 32% compared to the normal atmosphere. However, germination was reduced by at least 27% due to atmospheric modifications. Comparison of antioxidant enzyme activity (superoxide dismutases and catalases) with the oxidation profiles of biomolecules (proteins and lipids) showed that a decrease in catalase activity in the final days of culture coincided with an increase in the amount of oxidized lipids, showing that oxidative stress was a consequence of pulses of different concentrations of O₂. This is the first study describing oxidative stress induction by atmospheric modification, with practical implications for conidia production.     

Conidia production by <Emphasis Type="Italic">Beauveria bassiana</Emphasis> (for the biocontrol of a diamondback moth) during solid-state fermentation in a packed-bed bioreactor

Conidia of Beauveria bassiana CS-1, which have the potential for the control of the diamondback moth (Plutella xylostella), were produced by solid-state fermentation (SSF) using a packed-bed bioreactor with rice straw and wheat bran. As the packing density and the bed height were increased, the production of conidia decreased. In a packed-bed bioreactor under no aeration and no addition of polypropylene (PP) foam (control), the total average of conidia was 4.9 × 10⁸ g^-1. The production of conidia was affected more by the addition of PP foam as an inert support than forced aeration and was approx. 23 times higher than that of the control. The total average of conidia produced by B. bassiana was 1.1–1.2 × 10¹⁰ g^-1 . Revisions requested 6 September 2004/2 November 2004; Revisions received 1 November 2004/8 December 2004     

Production of anti‐inflammatory compounds in Sphaeralcea angustifolia cell suspension cultivated in stirred tank bioreactor

Sphaeralcea angustifolia is a plant used for the treatment of inflammatory processes. Scopoletin, tomentin, and sphaeralcic acid were identified as the compounds with anti‐inflammatory and immunomodulatory effects. Successful establishment of the cell culture in Erlenmeyer flasks has been reported previously. The aim of this study was to evaluate the ability of cells in suspension from S. angustifolia grown in a stirred tank bioreactor and demonstrate their capacity to produce bioactive compounds. Cells in suspension grown at 200 rpm reached a maximal cell biomass in dry weight at 19.11 g/L and produced 3.47 mg/g of sphaeralcic acid. The mixture of scopoletin and tomentin was only detected at the beginning of the culture (12.13 μg/g). Considering that the profile of dissolved oxygen during the cultures was lesser than 15%, it is possible that the low growth at 100 rpm could be due to oxygen limitations or to cell sedimentation. At 400 rpm, a negative effect on cell viability could be caused by the increase in the hydrodynamic stress, including the impeller tip, average shear rate, and Reynolds number. The sphaeralcic acid content in the cell suspension of S. angustifolia obtained in the bioreactor was two orders of magnitude greater than that reported for the culture grown in Erlenmeyer flasks.     

桦褐孔菌发酵及其提取物清除自由基活性的研究

用1,1-diphenyl-2-picryhydrazyl(DPPH)酶标仪法,对桦褐孔菌发酵液的甲醇提取物的自由基清除率进行了测定,发现该提取物具有较强的清除自由基的活性;进一步用DPPH薄层试验,结果发现该菌的CHCL3提取物中主要含有两个具清除自由基活性的组分.在此基础上,以清除自由基活性为指标,对桦褐孔菌液体发酵条件进行优化,发现当培养条件为:葡萄糖20g/L、甘油6mL/L、蛋白胨15g/L、CuSO4 0.005g/L、酪氨酸0.05g/L;种龄为7d、装液量为50mL/250mL、转速为180r/min、接种量为10%时,桦褐孔菌发酵液提取物的清除自由基活性最强.     

Enzymatic saccharification of cellulose in membrane reactors

The kinetics of enzymatic saccharification of ball-milled sugar-cane bagasse, sorghum stubble and peanut shells was studied and their conversions compared. Particle size analyses were performed on the bagasse sample and pure cellulose (Solka-Floc). It was revealed that most of the size reduction of cellulose particle took place between 0 5% conversion. Means of using commercially available ultrafiltration units as continuous-flow membrane reactors to reduce glucose inhibition were tested and compared using Solka-Floc as substrate. It was pointed out that a low conversion CSTR placed between a ball-mill and a hollow-fibre cartridge could reduce the cost of pretreatment and prevent possible blockage of hollow fibres.     

Reproducing shake flasks performance in stirred fermentors: production of alginates by Azotobacter vinelandii

Keeping equal the initial power drawn (0.27 W l(-1)) in shake flasks and in a stirred fermentor did not reproduce the behaviour of alginate production by Azotobacter vinelandii. A lower mean molecular weight (1.1x10(6) Da) of the polymer was obtained in the bioreactor as compared to that obtained in shake flasks (1.9x10(6) Da). The reasons for this can reside in the fact that the evolution of the power drawn in the shake flasks could be considerably different to that observed in the stirred bioreactor. A drastic drop in the specific power drawn is expected in the shake flasks as a consequence of the increased viscosity, which caused the liquid not following the movement of the shaker. This was supported by the fact that cultures developed in the fermentor at lower initial power drawn (as low as 0.027-0.056 W l(-1)) or in a culture in which the power drawn was deliberately reduced along cultivation, produced alginates with similar molecular characteristics as that obtained in shake flasks.