Reactor-Scale Cultivation of the Hyperthermophilic Methanarchaeon Methanococcus jannaschii to High Cell Densities

For the hyperthermophilic and barophilic methanarchaeon Methanococcus jannaschii, we have developed a medium and protocols for reactor-scale cultivation that improved the final cell yield per liter from ~0.5 to ~7.5 g of packed wet cells (~1.8 g dry cell mass) under autotrophic growth conditions and to ~8.5 g of packed wet cells (~2 g dry cell mass) with yeast extract (2 g liter⁻¹) and tryptone (2 g liter⁻¹) as medium supplements. For growth in a sealed bottle it was necessary to add Se to the medium, and a level of 2 μM for added Se gave the highest final cell yield. In a reactor M. jannaschii grew without added Se in the medium; it is plausible that the cells received Se as a contaminant from the reactor vessel and the H₂S supply. But, for the optimal performance of a reactor culture, an addition of Se to a final concentration of 50 to 100 μM was needed. Also, cell growth in a reactor culture was inhibited at much higher Se concentrations. These observations and the data from previous work with methanogen cell extracts (B. C. McBride and R. S. Wolfe, Biochemistry 10:4312–4317, 1971) suggested that from a continuously sparged reactor culture Se was lost in the exhaust gas as volatile selenides, and this loss raised the apparent required level of and tolerance for Se. In spite of having a proteinaceous cell wall, M. jannaschii withstood an impeller tip speed of 235.5 cms⁻¹, which was optimal for achieving high cell density and also was the higher limit for the tolerated shear rate. The organism secreted one or more acidic compounds, which lowered pH in cultures without pH control; this secretion continued even after cessation of growth.     

Optimal conditions for the production of sulfated polysaccharide by marine microalga Gyrodinium impudicum strain KG03

A marine microalga Gyrodinium impudicum strain KG03 produced sulfated exopolysaccharide designated as p-KG03, which showed a strong antiviral activity against encephalomyocarditis virus (EMCV). To optimize culture conditions for the production of p-KG03, mineral salts, vitamins, plant growth hormones, temperature, pH and light conditions were examined. From this study, M-KG03 medium for the maximum production of p-KG03 was suggested as follows; NH(4)Cl 75 microM, NaH(3)PO(4) 200 microM, NaHCO(3) 50 microM, Na(2)SO(4) 10 microM, FeCl(2) x 6H(2)O 10 microM, MnCl(2) x 4H(2)O 0.1 microM, vitamin B(12) 0.75 microg, naphthalene acetic acid (NAA) 7.5 microg and myo-inositol 200 mg per liter of aged sea water. The optimal temperature and pH were 22.5 degrees C and 8.0, respectively. The optimal light conditions of intensity and period were 150 microE m(-2) s(-1) and 16:8 h light:dark cycle. Finally, the cell growth and p-KG03 production were measured in one liter of M-KG03 medium with 1% CO(2) and 50 ml min(-1) of airflow using two liters airlift balloon type photobioreactor (ABTPR). At these optimal conditions, p-KG03 production and cell growth were 134.6+/-5.9 mg l(-1) and 123,076+/-1,597 cells ml(-1), respectively, representing a 7.7 and 5.1 times compared with f/2 medium with Erlenmeyer flask culture (p-KG03 production 17.5+/-1.3 mg l(-1) and cell growth 24,311+/-1,291 cells ml(-1)).     

Evaluation of Mut+ and MutS Pichia pastoris phenotypes for high level extracellular scFv expression under feedback control of the methanol concentration

Extracellular secretion of over 4 g x L(-1) of the A33 scFv antibody fragment was achieved in Pichia pastoris at the 10 L bioreactor scale using minimal medium and feedback control of the methanol concentration. Since methanol acts as both inducer and carbon source, its close regulation is a crucial factor in achieving optimal fermentation conditions. The antibody fragment production levels of both Mut+ and MutS phenotypes were compared in a bioreactor under closed-loop PID control of the methanol level. As expected, the MutS phenotype has a growth rate lower than that of the Mut+ (0.37 vs 1.05 d(-1)) when growing under methanol. However, protein productivity and cell yield on substrate are almost double that of the Mut+ (18.2 vs 9.3 mg A33 sc per gram of methanol). Induction at wet cell weight of 350 g x L(-1) for the MutS also has a positive effect on the final product concentration. Both Mut+ and MutS phenotypes reach a maximum biomass density around 450 g x L(-1) wet cell weight, independent of methanol concentration, reactor scale, or induction density. This reactor configuration allows for reproducible fermentation schemes with different Pichia pastoris phenotypes with AOX promoters, without prior knowledge of the culture growth parameters.     

Growth kinetics of vitis vinifera cell suspension cultures: I. Shake flask cultures

Vitis vinifera cell suspension cultures carried out in shake flasks were closely examined for biomass growth and cell division in relation to carbohydrate, NH(4), NO(3)PO(4), and dissolved oxygen (DO)consumption. After inoculation, the oxygen uptake rate of the cultures measured on-tine was observed to increase continuously to a maximum value of 3.8 mmol O(2)L(-1)h(-1) at day 7 when cell division ceased and dissolved oxygen reached its lowest level of 17% air saturation. During this first phase of growth, the specific oxygen uptake rate remained constant at approximately 0.6 mmol 02 O(2) g(-1) dw h(-1)or approximately 2.2 mumol O(2), (10(6) cells)(-1) h(-1) whereas dry biomass concentration increased exponentially from 1.5 to 6.0 g dw L(-1). Thereafter, dry biomass concentration increased linearly to approximately 14 g dw L(-1) at day 14 following nitrate and carbohydrate uptake. During this second phase of growth, the biomass wet-to-dry weight ratio was found to increase in an inverse relationship with the estimated osmotic pressure of the culture medium. This corresponded to inflection points in the dry and wet biomass concentration and packed cell volume curves. Furthermore, growth and nutrient uptake results suggest that extracellular ammonium or phosphate ion availability may limit cell division. These findings indicate that cell division and biomass production of plant cell cultures may not always be completely associated, which suggests important new avenues to improve their productivity. (c) 1995 John Wiley & Sons, Inc.     

The in vitro retardation of porcine cataractogenesis by the calpain inhibitor, SJA6017

Calpain inhibitors show the potential to serve as non-surgical alternatives in treating diabetic cataract and other types of these disorders. Here, we have tested the recently developed calpain inhibitor, SJA6017, for its ability to inhibit cataractogenesis in porcine lenses. These lenses were incubated in increasing levels of extralenticular calcium (Ca2+; 5-30 mM). Atomic absorption spectroscopy was used to determine total internal lens Ca2+ and a correlation between porcine lens Ca2+ uptake and levels of lens opacification were found with a total internal lens Ca2+ level of 5.8 microM Ca2+ g(-1) wet lens weight corresponding to the onset of catarctogenesis. A total internal lens Ca2+ level of 8.0 microM Ca2+ g(-1) wet lens weight corresponded to cataract occupying approximately 70% of the lens cell volume. This degree of cataract was reduced by approximately 40%, when SJA6017 (final concentration 0.8 microM) was included in the extralenticular medium, suggesting that the Ca2+-mediated activation of calpains may be involved in the observed opacification. Supporting this suggestion atomic absorption spectroscopy showed that the effect of SJA6017 (final concentration 0.8 microM) on lens opacification was not due to the compound restricting porcine lens Ca2+ uptake. The results indicate that calpain-induced cataractogenesis is dependent on extracellular Ca2+ and the calpain inhibitor SJA6017 (0.8 microM) had no significant effect on Ca2+ uptake by lens. Its inhibitory effect on lens opacification may be due to a direct action on the activity of calpain.     

Enhanced Yields of Iron-Oxidizing Bacteria by In Situ Electrochemical Reduction of Soluble Iron in the Growth Medium

An electrochemical apparatus for culturing chemolithotrophic bacteria that respire aerobically on ferrous ions is described. Enhanced yields of the bacteria were achieved by the in situ electrochemical reduction of soluble iron in the growth medium. When subjected to a direct current of 30 A for 60 days, a 45-liter culture of Thiobacillus ferrooxidans grew from 6 × 10⁷ to 9.5 × 10⁹ cells per ml. Growth of the bacterium within the electrolytic bioreactor was linear with time. A final cell density corresponding to 4.7 g of wet cell paste per liter was achieved, and a total of 320 g of wet cell paste was harvested from one culture. The apparatus was designed to deliver protons concomitantly with electrons; therefore, the pH of the culture remained stable at 1.6 ± 0.1 for the duration of growth. This laboratory-scale apparatus may be readily adapted to pilot or production scale. It is thus anticipated that abundant numbers of iron-oxidizing bacteria may be obtained for both fundamental and applied studies.     

Protocols for production of selenomethionine-labeled proteins in 2-L polyethylene terephthalate bottles using auto-induction medium

Protocols have been developed and applied in the high-throughput production of selenomethionine labeled fusion proteins using the conditional Met auxotroph Escherichia coli B834. The large-scale growth and expression uses a chemically defined auto-induction medium containing 125 mg L(-1) selenomethionine, salts and trace metals, other amino acids including 10 mg L(-1) of methionine, vitamins except vitamin B12, and glucose, glycerol, and alpha-lactose. A schematic for a shaker rack that can hold up to twenty-four 2-L polyethylene terephthalate beverage bottles in a standard laboratory refrigerated floor shaker is provided. The growth cycle from inoculation of the culture bottle through the growth, induction, and expression was timed to take approximately 24 h. Culture growth in the auto-induction medium gave an average final optical density at 600 nm of approximately 6 and an average wet cell mass yield of approximately 14 g from 2 L of culture in greater than 150 expression trials. A simple method for visual scoring of denaturing electrophoresis gels for total protein expression, solubility, and effectiveness of fusion protein proteolysis was developed and applied. For the favorably scored expression trials, the average yield of purified, selenomethionine-labeled target protein obtained after proteolysis of the fusion protein was approximately 30 mg. Analysis by mass spectrometry showed greater than 90% incorporation of selenomethionine over a approximately 8-fold range of selenomethionine concentrations in the growth medium, with higher growth rates observed at the lower selenomethionine concentrations. These protein preparations have been utilized to solve X-ray crystal structures by multiwavelength anomalous diffraction phasing.     

Perfusion culture of hybridoma cells for hyperproduction of IgG(2a) monoclonal antibody in a wave bioreactor-perfusion culture system

A novel wave bioreactor-perfusion culture system was developed for highly efficient production of monoclonal antibody IgG2a (mAb) by hybridoma cells. The system consists of a wave bioreactor, a floating membrane cell-retention filter, and a weight-based perfusion controller. A polyethylene membrane filter with a pore size of 7 microm was floating on the surface of the culture broth for cell retention, eliminating the need for traditional pump around flow loops and external cell separators. A weight-based perfusion controller was designed to balance the medium renewal rate and the harvest rate during perfusion culture. BD Cell mAb Medium (BD Biosciences, CA) was identified to be the optimal basal medium for mAb production during batch culture. A control strategy for perfusion rate (volume of fresh medium/working volume of reactor/day, vvd) was identified as a key factor affecting cell growth and mAb accumulation during perfusion culture, and the optimal control strategy was increasing perfusion rate by 0.15 vvd per day. Average specific mAb production rate was linearly corrected with increasing perfusion rate within the range of investigation. The maximum viable cell density reached 22.3 x 105 and 200.5 x 105 cells/mL in the batch and perfusion culture, respectively, while the corresponding maximum mAb concentration reached 182.4 and 463.6 mg/L and the corresponding maximum total mAb amount was 182.4 and 1406.5 mg, respectively. Not only the yield of viable cell per liter of medium (32.9 x 105 cells/mL per liter medium) and the mAb yield per liter of medium (230.6 mg/L medium) but also the mAb volumetric productivity (33.1 mg/L.day) in perfusion culture were much higher than those (i.e., 22.3 x 105 cells/mL per liter medium, 182.4 mg/L medium, and 20.3 mg/L.day) in batch culture. Relatively fast cell growth and the perfusion culture approach warrant that high biomass and mAb productivity may be obtained in such a novel perfusion culture system (1 L working volume), which offers an alternative approach for producing gram quantity of proteins from industrial cell lines in a liter-size cell culture. The fundamental information obtained in this study may be useful for perfusion culture of hybridoma cells on a large scale.     

Production of polysaccharides by Silene vulgaris callus culture depending on carbohydrates of the medium

Sources of carbohydrate nutrition such as sucrose, glucose, and galactose, with the exception of arabinose, were shown to influence positively callus growth and polysaccharide (pectin silenan and acidic arabinogalactan) biosynthesis. Galactose was found to cause a stimulatory effect on yield and productivity of arabinogalactan. Low concentrations of sucrose failed to support the cell growth and polysaccharide biosynthesis. Increasing sucrose concentrations led to biomass accumulation but failed to enhance efficiency of the substrate utilization. The optimal medium for the campion cell culture growth was found to be one containing 30 g/liter of sucrose or a mixture of sucrose with glucose (in 15 g/liter). Increasing sucrose concentrations in the medium from 30 to 100 g/liter failed to significantly influence the polysaccharide yields while the polysaccharide productivity per liter of the medium grew due to promotion of culture productivity in biomass. Variations of the carbon sources in the nutrient media were shown to influence insignificantly the biochemical characteristics of arabinogalactan and silenan while an increase in the sucrose concentration to 50-100 g/liter led to a diminution of the galacturonic acid content in silenan and to changes in contents of the neutral monosaccharide residues in silenan and arabinogalactan.     

重组大肠杆菌产普鲁兰酶的高密度发酵工艺研究

以表达普鲁兰酶的重组大肠杆菌作为出发菌株,在摇瓶培养的基础上,建立了大肠杆菌工程菌产普鲁兰酶的高密度发酵工艺。通过测定细胞密度、细胞干重、分离菌体可溶性成分与不溶性成分及SDS-PAGE电泳,分析重组大肠杆菌的生长和普鲁兰酶的表达情况。摇瓶试验使用合成培养基和LB培养基,重组大肠杆菌在合成培养基生长较慢,诱导5 h的普鲁兰酶表达量高于LB培养基,包涵体比例低于LB培养基。重组大肠杆菌的高密度发酵使用合成培养基,补料阶段采用指数流加的工艺,在设定细胞的比生长速率为0.12的前提下,限制补料中碳源的供应,以阻止乙酸的产生。当细胞密度OD600达到70.0开始诱导,最终细胞密度为每升53.3 g细胞干重,细胞内可溶性普鲁兰酶为每升1.35 g。     

表达重组葡激酶-水蛭素融合蛋白的大肠杆菌工程菌的高密度培养

采用溶氧反馈的分批培养流加补料的方法高密度培养重组大肠杆菌BL21(DE3)生产重组葡激酶-水蛭素融合蛋白。通过摇瓶培养对菌种和培养条件的初步筛选,采用溶氧反馈的流加补料策略,进行了5L发酵罐的合成培养基和复合培养基的发酵工艺的研究。通过对培养条件的不断优化,重组葡激酶-水蛭素融合蛋白在大肠杆菌BL21(DE3)里得到了高效表达,菌体密度最终达到115g/L(WCW)以上,可溶性重组融合蛋白占菌体总蛋白的30%以上,含量约为1.1~1.2g/L。5L发酵罐的发酵工艺参数在40L发酵罐中进行了放大培养,结果表明该工艺能有效的放大,可适用于工业生产。     

High cell density cultivation of Pseudomonas oleovorans: growth and production of poly (3-hydroxyalkanoates) in two-liquid phase batch and fed-batch systems

Pseudomonas oleovorans is able to accumulate poly(3-hydroxyalkanoates) (PHAs) under conditions of excess n-alkanes, which serve as sole energy and carbon source, and limitation of an essential nutrient such as ammonium. In this study we aimed at an efficient production of these PHAs by growing P. oleovorans to high cell densities in fed-batch cultures.To examine the efficiency of our reactor system, P. oleovorans was first grown in batch cultures using n-octane as growth substrate and ammonia water for pH regulation to prevent ammonium limiting conditions. When cell growth ceased due to oxygen limiting conditions, a maximum cell density of 27 g .L(-1) dry weight was obtained. When the growth temperature was decreased from the optimal temperature of 30 degrees -18 degrees C, cell growth continued to a final cell density of 35 g . L(-1) due to a lower oxygen demand of the cells at this lower incubation temperature.To quantify mass transfer rates in our reactor system, the volumetric oxygen transfer coefficient (k(L)a) was determined during growth of P. oleovorans on n-octane. Since the stirrer speed and airflow were increased during growth of the organism, the k(L)a also increased, reaching a constant value of 0.49 s(-1) at maximum airflow and stirrer speed of 2 L . min(-1) and 2500 rpm, respectively. This k(L)a value suggests that oxygen transfer is very efficient in our stirred tank reactor.Using these conditions of high oxygen transfer rates, PHA production by P. oleovorans in fed-batch cultures was studied. The cells were first grown batchwise to a density of 6 g . L(-1), after which a nutrient feed, consisting of (NH(4))(2)SO(4) and MgSO(4), was started. The limiting nutrient ammonium was added at a constant rate of 0.23 g NH(4) (+) per hour, and when after 38 h the feed was stopped, a biomass concentration of 37.1 g . L(-1) was obtained. The Cellular PHA content was 33% (w/w), which is equal to a final PHA yield of 12.1 g . L(-1) and an overall PHA productivity of 0.25 g PHA produced per liter medium per hour. (c) 1993 John Wiley & Sons, Inc.     

Docosahexaenoic acid ethyl esters from Isochrysis galbana

In order to produce docosahexaenoic acid (DHA), a culture of the microalgal strain Isochrysis galbana was implemented. In Erlenmeyer flasks, a natural seawater medium, the Provasoli 1/3 medium, was compared to the classical Jones medium for DHA production. The Provasoli 1/3 medium stimulated growth (0.44 d(-1)), but influenced DHA accumulation negatively (0.240 pg cell(-1)). However, DHA production per liter of culture medium were of the same order of magnitude with both media (0.961 mg l(-1)). In a 2-l bioreactor, DHA production per liter of culture medium did not increase significantly between 4 and 8 days of culture. With a view to optimize DHA productivity, cells should be harvested at the end of exponential phase i.e. after 4 days of culture. Two strategies were then attempted to produce DHA ethyl esters. First, lipids from I. galbana were submitted to lipase-catalyzed transesterification with ethanol. Secondly, fatty acids from I. galbana were submitted to lipase catalyzed esterification with ethanol. In both cases, lipase from Candida antarctica was shown to be the best candidate, among the five tested, with conversion yields of 20 and 60% after 24 h of transesterification and esterification respectively.     

Degradation of phenol by Pseudomonas putida ATCC 11172 in continuous culture at different ratios of biofilm surface to culture volume.

Pseudomonas putida ATCC 11172 was grown in continuous culture with phenol as the only carbon and energy source; a culture practically without biofilm was compared with biofilm cultures of differing surface area/volume ratios. The biofilm did not significantly affect the maximal suspended cell concentration in the effluent, but it increased the maximal phenol reduction rate from 0.23 g/liter per h (without biofilm) to 0.72 g/liter per h at the highest biofilm level (5.5 cm2 of biofilm surface per ml of reactor volume). The increase in phenol reduction rate was linear up to the surface area/volume ratio of 1.4 cm2/ml. The continuous cultures with biofilms could tolerate a higher phenol concentration of the medium (3.0 g/liter) than the nonbiofilm system (2.5 g/liter). At higher dilution rates an intermediate product, 2-hydroxymuconic semialdehyde, accumulated in the culture. When the biomass of the effluent started to decrease, the concentration of 2-hydroxymuconic semialdehyde reached a peak value. We conclude that biofilms in continuous culture have the potential to enhance the aerobic degradation of aromatic compounds.     

Degradation of phenol by Pseudomonas putida ATCC 11172 in continuous culture at different ratios of biofilm surface to culture volume

Pseudomonas putida ATCC 11172 was grown in continuous culture with phenol as the only carbon and energy source; a culture practically without biofilm was compared with biofilm cultures of differing surface area/volume ratios. The biofilm did not significantly affect the maximal suspended cell concentration in the effluent, but it increased the maximal phenol reduction rate from 0.23 g/liter per h (without biofilm) to 0.72 g/liter per h at the highest biofilm level (5.5 cm2 of biofilm surface per ml of reactor volume). The increase in phenol reduction rate was linear up to the surface area/volume ratio of 1.4 cm2/ml. The continuous cultures with biofilms could tolerate a higher phenol concentration of the medium (3.0 g/liter) than the nonbiofilm system (2.5 g/liter). At higher dilution rates an intermediate product, 2-hydroxymuconic semialdehyde, accumulated in the culture. When the biomass of the effluent started to decrease, the concentration of 2-hydroxymuconic semialdehyde reached a peak value. We conclude that biofilms in continuous culture have the potential to enhance the aerobic degradation of aromatic compounds.     

Optimization of Escherichia coli cultivation methods for high yield neuropeptide Y receptor type 2 production

The recombinant expression of human G protein-coupled receptors usually yields low production levels using commonly available cultivation protocols. Here, we describe the development of a high yield production protocol for the human neuropeptide Y receptor type 2 (Y2R), which provides the determination of expression levels in a time, media composition, and process parameter dependent manner. Protein was produced by Escherichia coli in a defined medium composition suitable for isotopic labeling required for investigations by nuclear magnetic resonance spectroscopy. The Y2 receptor was fused to a C-terminal 8x histidine tag by means of the pET vector system for easy one-step purification via affinity chromatography, yielding a purity of 95-99% for every condition tested, which was determined by SDS-PAGE and Western blot analysis. The Y2 receptor was expressed as inclusion body aggregates in complex media and minimal media, using different carbon sources. We investigated the influences of media composition, temperature, pH, and set specific growth rate on cell behavior, biomass wet weight specific and culture volume specific amounts of the target protein, which had been identified by inclusion body preparation, solubilization, followed by purification and spectrometric determination of the protein concentration. The developed process control strategy led to very high reproducibility of cell growth and protein concentrations with a maximum yield of 800 μg purified Y2 receptor per gram wet biomass when glycerol was used as carbon source in the mineral salt medium composition (at 38 °C, pH 7.0, and a set specific growth rate of 0.14 g/(gh)). The maximum biomass specific amount of purified Y2 receptor enabled the production of 35 mg Y2R per liter culture medium at an optical density (600 nm) of 25.     

Cytidine deaminase levels in cultured mammalian cell lines measured by the growth tests and enzyme assays

We developed a test medium for cytidine deaminase in order to examine the distribution of this enzyme in cultured cell lines. The growth of various mammalian cell lines was tested in culture medium containing 2 microM pyrazofurin and 100 microM cytidine. Enzymological assays for the enzyme also were made spectrophotometrically with cell extracts. A good correlation was found between results of cell growth tests and the levels of enzyme activity. Twelve of twenty cell lines were killed in the test medium, but the remaining lines showed good growth. The levels of enzyme activities were lower in the former lines than in the latter. The critical level of enzyme activity required to support cell growth was approximately 30 units per mg protein. These findings indicate that culture medium containing 2 microM pyrazofurin and 100 microM cytidine serves as a test medium for cytidine deaminase. The possibility that the cytidine deaminase may be useful in determining the embryonic origin of cultured cell lines is discussed, based on the growth properties of various cultured cell lines in the test medium.     

Selenium increases hydrogenase expression in autotrophically cultured Bradyrhizobium japonicum and is a constituent of the purified enzyme.

We have investigated the effect of added selenite on autotrophic growth and the time course of hydrogen oxidation derepression in Bradyrhizobium japonicum 122DES cultured in a medium purified to remove selenium compounds. In addition, hydrogenase was purified to near homogeneity and examined for the specific incorporation of Se into the enzyme. The addition of Se at 0.1 microM significantly increased total cell protein and hydrogenase specific activity of harvested cells. Also, the addition of SeO3(2-) enhanced the time course of hydrogenase derepression by 133%, whereas VO3, AsO2(2-), SO2(2-), and TeO3(2-) failed to substantially affect hydrogenase derepression. During the final chromatographic purification of hydrogenase, a striking coincidence in peaks of protein content, Se radioactivity, and hydrogenase activity of fractions was obtained. The total Se content expressed per milligram of protein increased manyfold during the purification procedure. The mean Se content of the purified hydrogenase was 0.56 +/- 0.13 mol of Se per mol of enzyme. These results indicate that Se is an important element in the H2 metabolism of B. japonicum and that hydrogenase from B. japonicum is a seleno protein.     

Formation of Short-Chain Fatty Acids from H(2) and CO(2) by a Mixed Culture of Bacteria

The biological utilization of CO(2) and H(2) for the formation of short-chain fatty acids was studied by using a mixed culture of bacteria. Optimization of a medium was carried out in continuous culture to identify limiting factors which controlled growth and production of organic acids. The optimal pH for growth and acid production was 7.0 at 37 degrees C; the maximal cell concentration obtained was 5.9 g of cells per liter (dry weight), and the maximal amount of volatile acids formed was 4.7 g/liter, with acetic acid as the predominant acid. With the optimized medium, it was found that the rate of transfer of hydrogen or carbon dioxide, or both, from gas to liquid was the limiting factor which controlled growth and production of acids.     

Toluene biofiltration by the fungus Scedosporium apiospermum TB1

The performance of biofilters inoculated with the fungus Scedosporium apiospermum was evaluated. This fungus was isolated from a biofilter which operated with toluene for more than 6 months. The experiments were performed in a 2.9 L reactor packed with vermiculite or with vermiculite-granular activated carbon as packing material. The initial moisture content of the support and the inlet concentration of toluene were 70% and 6 g/m3, respectively. As the pressure drop increased from 5-40 mm H2O a strong initial growth was observed. Stable operation was maintained for 20 days with a moisture content of 55% and a biomass of 33 mg biomass/g dry support. These conditions were achieved with intermittent addition of culture medium, which permitted a stable elimination capacity (EC) of 100 g/m3(reactor)h without clogging. Pressure drop across the bed and CO2 production were related to toluene elimination. Measurement of toluene, at different levels of the biofilter, showed that the system attained higher local EC (200 g/m3(r)h) at the reactor outlet. These conditions were related to local humidity conditions. When the mineral medium was added periodically before the EC decreases, EC of approximately 258 g/m3(r)h were maintained with removal efficiencies of 98%. Under these conditions the average moisture content was 60% and 41 mg biomass/g dry support was produced. No sporulation was observed. Evaluation of bacterial content and activities showed that the toluene elimination was only due to S. apiospermum catabolism.