Continuous acetone-butanol fermentation: influence of vitamins on the metabolic activity of Clostridium acetobutylicum

Summary A detailed investigation was undertaken to examine the influence of biotin and paminobenzoic acid (PABA) in chemostat cultures of Clostridium acetobutylicum ATCC 824. Initiation of chemostat cultures with a basic synthetic medium (biotin 0.01 mg l^–1; PABA 1.0 mg l^–1) have resulted in a low biomass together with a low specific rate of solvent production. A different picture emerged on elevating the concentration of both vitamins 8-fold: biomass and specific rates (solvent production, glucose consumption) were increased and a solvent productivity of 2.54 g l^–1 h^–1 at the solvent concentration of 13.1 g l^–1 was achieved. It has also been shown that PABA was the only limiting factor for the metabolism of Clostridium acetobutylicum in the basic synthetic medium and that the optimised concentration was 8 mg l^–1 in the chemostat cultures with the growth conditions employed.     

Formaldehyde Production by Cells of a Mutant of Candida boidinii S2 Grown in Methanol-limited Chemostat Culture

Formaldehyde production was investigated with cells of a mutant, AOU-1, of a methanol yeast, Candida boidinii S2 grown in methanol-limited chemostat culture. The highest productivity was shown with cells from the culture at a dilution rate of 0.075 hr^-1, when cells had the highest activity of alcohol oxidase and almost minimum activity of formaldehyde dehydrogenase. Under optimal reaction conditions, 950 mm formaldehyde was produced in 10-hr reaction with the cells. By the chemostat culture, not only formaldehyde productivity but also cell productivity was improved in comparison with batch culture. A maximum cell productivity of 0.2 g · liter^-1 · hr^-1 and a cell yield of 47% were obtained.     

Lipase production by recombinant strains of <Emphasis Type="Italic">Aspergillus niger</Emphasis> expressing a lipase-encoding gene from <Emphasis Type="Italic">Thermomyces lanuginosus</Emphasis>

Two recombinant strains of Aspergillus niger (NW 297-14 and NW297-24) producing a heterologous lipase from Thermomyces lanuginosus were constructed. The heterologous lipase was expressed using the TAKA amylase promoter from Aspergillus oryzae. The production kinetics of the two strains on different carbon sources in batch and carbon-limited chemostat cultivations were evaluated. In batch cultivations, the highest total product yield coefficient (Y_{xp total}), given as the sum of extracellular and intracellular yields, was obtained during growth on glucose for the transformant strain NW297-24 (5.7±0.65 KU/g DW), whereas the highest total product yield coefficient was obtained during growth on maltose for the transformant strain NW297-14 (6.3±0.02 KU/g DW). Both transformants were evaluated in glucose-limited chemostat cultures. Strain NW297-14 was found to be the best producer and was thus employed for further analysis of the influence of carbon source in chemostat cultures. Here, the highest total specific lipase productivity (r_{p total}, the sum of extracellular and intracellular lipase productivity) was found to be 1.60±0.81 KU/g DW/h in maltose-limited chemostats at a dilution rate of 0.08 h^–1, compared with a total specific lipase productivity of 1.10±0.41 KU/g DW/h in glucose-limited chemostats. At the highest specific productivity obtained in this study, the heterologous enzyme accounted for about 1% of all cellular protein being produced by the cells, which shows that it is possible to obtain high productivities of heterologous fungal enzymes in A. niger. However, SDS-PAGE analysis showed that most of the produced lipase was bound to the cell wall.     

Influence of dilution rate on the morphology and technological properties ofLactobacillus delbrueckii subsp.bulgaricus

Lactobacillus delbrueckii subsp.bulgaricus ATCC 11842 was grown in a chemostat at 45°C and pH 5.5 using glucose as the carbon source, with the aim of optimizing biomass production. Cells were grown in a complex medium under nitrogen. At dilution rates lower than 0.18h^–1, it was difficult to keep steady-state conditions and pleomorphic forms were observed. The addition of 30mM Ca²⁺ and Mn²⁺ reverted the cells to normal shape: 30mM Mg²⁺ had no effect. Increasing the dilution rate resulted in normal morphology without the addition of any cations. Under these conditions, a maximum productivity of 1.24g dry biomass 1^–1 h^–1 was obtained. The maximum growth yield, corrected for maintenance, was 30g biomass mol^–1 glucose and the maintenance energy was 0.26g glucose g^–1 biomass h^–1. Lactate was the main fermentation product at all glucose concentrations used in the fed medium. Cells grown at high dilution rates had normal technological properties (acid production and proteolysis) when tested in milk.     

Enzyme production in continuous cultivation by the thermophilic fungus, Thermomyces lanuginosus

The production of extracellular enzymes by the thermophilic fungus Thermomyces lanuginosus was studied in chemostat cultures at a dilution rate of 0.08 h^–1 in relation to variation in the ammonium concentration in the feed medium. Under steady state conditions, three growth regimes were recognised and the production of several extracellular enzymes from T. lanuginosus was recorded under different nutrient limitations ranging from nitrogen limitation to carbon/energy limitation. The range and the production of carbohydrate hydrolysing enzymes and lipase increased from Regime I (NH₄Cl 600 mg l^–1) to Regime III (NH₄CI 1200 mg l^–1), whereas production of protease was highest in Regime II (600 mg l^–1 < NH₄Cl <1200 mg l^–1).     

Lactase production in continuous culture by Trichoderma reesei Rut-C30

Summary Trichoderma reesei Rut-C30 was found to produce extracellular lactase when grown on lactose medium. Maximum enzyme levels in continuous culture were observed at dilution rates (D) between 0.02 and 0.027 hr^-1. The enzyme productivity reached 27.3 U/L hr at D = 0.027 hr^-1. Lactase synthesis appears to be inducible and subject to catabolite repression. Optimal growth temperature and pH for enzyme production were 28°C and pH 5. Maximum enzyme activity was observed at 63°C and pH 4.6. The apparent K_m, based on the nitrophenyl-galactopyranoside assay was estimated as 0.4 mM. The enzyme is suitable for lactose hydrolysis in acid whey.     

Influence of environmental factors on endo-β-1,4-glucanase production by Bacillus HR68, isolated from a Zimbabwean hot spring

The production of endo-β-1,4-glucanase by a Bacillus strain isolated from a hot spring in Zimbabwe was studied in batch culture, chemostat culture, and carbon dioxide-regulated auxostat (CO₂-auxostat). The bacteria produced the enzyme in the presence of excess glucose or sucroso, but not under carbon-limited conditions in a chemostat using mineral medium. There was a specific growth rate dependent linear increase in enzyme production in glucose excess, nitrogen-limited chemostat cultures. A high specific growth rate of 2.2 h^-1 and a high rate of enzyme production of 362 nkat (mg dry mass h)^-1 were attained under nutrient rich conditions in the CO₂-auxostat. The bacteria had the highest specific growth rate and endo-β-1,4-glucanase enzyme production at 50° C. The maximum specific growth rate and the rate of enzyme production increased when yeast extract and tryptone were added in increasing amounts to the mineral medium used for cultivation in separate experiments. Increasing the glucose concentration in the CO₂-auxostat cultures increased the rate of enzyme production but did not affect the specific growth rate.     

Performance of batch, fed-batch, and continuous A-B-E fermentation with pH-control

Batch, fed-batch, and continuous A-B-E fermentations were conducted and compared with pH controlled at 4.5, the optimal range for solvent production. While the batch mode provides the highest solvent yield, the continuous mode was preferred in terms of butanol yield and productivity. The highest butanol yield and productivity found in the continuous fermentation at dilution rate of 0.1 h⁻¹ were 0.21 g-butanol/g-glucose and 0.81 g/L/h, respectively. In the continuous and fed-batch fermentation, the time needed for passing acidogenesis to solventogenesis was an intrinsic hindrance to higher butanol productivity. Therefore, a low dilution rate is suggested for the continuous A-B-E fermentation, while the fed-batch mode is not suggested for solvent production. While 3:6:1 ratio of acetone, butanol, and ethanol is commonly observed from A-B-E batch fermentation by Clostridium acetobutylicum when the pH is uncontrolled, up to 94% of the produced solvent was butanol in the chemostat with pH controlled at 4.5.     

Chemostat production of pediocin SM‐1 by Pediococcus pentosaceus Mees 1934

Production of the bacteriocin pediocin SM‐1 by Pediococcus pentosaceus Mees 1934 was investigated in pH‐controlled batch and chemostat cultures using a complex medium containing glucose, sucrose or fructose. In chemostat cultures operated at 150 rpm, 30°C, 60% dissolved oxygen tension, pH 6.5, and D = 0.148 h^?1, the pediocin titer reached 185 AU/mL representing an increase of 32% compared with batch cultures in which glucose was used as the carbon source. Pediocin biosynthesis was markedly affected by the growth rate of the producer microorganism. For all carbon sources tested, pediocin production appeared to take place only at dilution rates lower than μ_max. However, only glucose supported production at the very low dilution rate of 0.05 h^?1 indicating a direct regulation of pediocin biosynthesis by the carbon source. Glucose supported higher biomass productivity and higher pediocin titers and yields compared with the other sugars used. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1481–1486, 2015     

Production of the macrolide antibiotic tylosin in batch and chemostat cultures

The production of tylosin and related compounds by Streptomyces fradiae NRRL 2702 was studied in batch and chemostat cultures using a soluble synthetic medium. In batch culture, a trophophase–idiophase kinetic pattern was observed with tylosin, macrocin, and relomycin accumulating in the idiophase. When the organism was grown in chemostat culture, the specific rate of production of tylosin and related compounds (q_tylosin) was found to be a function of the growth rate. The maximum value of (q_tylosin) was observed when D = 0.017 hr^?1. At this growth rate only tylosin and relomycin accumulated in the medium. By varying the concentration of glucose in the ingoing medium it was possible to study the effects of glucose on tylosin synthesis in chemostat cultures. At a growth rate of 0.017 hr^?1, the maximum value of q_tylosin was 0.71 mg tylosin/g dry weight (DW)/hr when the glucose uptake rate was 7 mg glucose/g DW-hr. This value of q_tylosin was 40% greater than the maximum q_tylosin observed in batch culture. When glycerol was substituted for glucose in the medium, it was possible in chemostat culutures to get values of q_tylosin approximately 20% greater than those obtained with glucose at the same uptake rate. By varying the concentration of sodium glutamate in the ingoing medium it was possible to show that increasing the specific uptake rate of sodium glutamate increased the values of q_tylosin obtained. Similar chemostat experiments where the inorganic phosphate concentration in the ingoing medium was varied showed that increased the uptake of phosphate decreased the values of q_tylosin obtained. Also increasing the uptake rate of phosphate increased the relomycin-to-tylosin ratio. By taking into consideration the suppressing effects of glucose and the stimulating effects of sodium glutamate on tylosin synthesis, it was possible to formulate a medium that resulted in a value of q_tylosin of 1.1 mg/g/hr being obtained at a growth rate of 0.03 hr^?1. Batch fermentations with this medium did not follow a trophophase–idiophase kinetic pattern, but instead tylosin was actively synthesized during a period of rapid mycelial growth.     

Isolation of a yeast-lyzing Arthrobacter species and the production of the lytic enzyme complex in batch and continuous-flow fermentors

A gram-negative bacterium strongly lytic toward living cells of the food yeast Saccharomyces fragilis was isolated by continuous-flow enrichment from compost. The organism was identified as a species of Arthrobacter. The extracellular lytic enzyme complex produced by this bacterium contained β-1,3-glucanase, mannan mannohydrolase, and proteolytic activities. The polysaccharases were inducible by whole yeast cells. In chemostat cultures on chemically defined media, synthesis of the polysaccharases was very slight and only detectable at dilution rates below 0.02 hr^?1. Enzyme production in defined media was not solely dependent on growth rate but also was influenced by the growth limiting substrate and the culture history. The production of individual depolymerases and of the lytic activity was studied in batch and chemostat cultures containing yeast as the limiting substrate. The maximum specific growth rate of the Arthrobacter under these conditions was 0.22 hr^?1. β-1,3-Glucanase and proteolytic activities were synthesized by exponentially growing bacteria but maximum lytic titers did not develop until the specific growth rate was declining, at which time mannan mannohydrolase syntheses was induced. In yeast limited chemostats polysaccharase syntheses were greatest at the lowest dilution rates examined, namely 0.02 hr^?1. Further optimization of enzyme production was achieved by feeding the Arthrobacter culture to a second-stage chemostat. A comparison of lytic enzyme productivities in batch and chemostat cultures has been made.     

Denitrification of nitrate and nitric acid with methanol as carbon source

Summary A methanol/nitrate-medium and anaerobic conditions yielded an enrichment culture which consisted ofHyphomicrobium andParacoccus. This mixed culture proved to be very effective in denitrification of solutions containing high concentrations of nitrate and free nitric acid when grown in a chemostat (D=0.04 h^-1). With 0.1 mol/l nitric acid solution as feed medium the pH in the culture vessel adjusted itself to 5.8. For the reduction of 1 g NO₃–N 2.6 g methanol were consumed and 0.56 g cells were produced.     

Enhanced iturin A production by <Emphasis Type="Italic">Bacillus subtilis</Emphasis> and its effect on suppression of the plant pathogen <Emphasis Type="Italic">Rhizoctonia solani</Emphasis>

The behavior of Streptomyces peucetius var. caesius N47 was studied in a glucose limited chemostat with a complex cultivation medium. The steady-state study yielded the characteristic constants μ _max over 0.10 h⁻¹, Y _XS 0.536 g g⁻¹, and m_S 0.54 mg g⁻¹ h⁻¹. The product of secondary metabolism, ɛ-rhodomycinone, was produced with characteristics Y _PX 12.99 mg g⁻¹ and m _P 1.20 mg g⁻¹ h⁻¹. Significant correlations were found for phosphate and glucose consumption with biomass and ɛ-rhodomycinone production. Metabolic flux analysis was conducted to estimate intracellular fluxes at different dilution rates. TCA, PPP, and shikimate pathway fluxes exhibited bigger values with production than with growth. Environmental perturbation experiments with temperature, airflow, and pH changes on a steady-state chemostat implied that an elevation of pH could be the most effective way to shift the cells from growing to producing, as the pH change induced the biggest transient increase to the calculated ɛ-rhodomycinone flux.     

Prodigiosin formation by Serratia marcescens in a chemostat

In a study of the control of metabolite formation, prodigiosin production by Serratia marcescens was used as a model. Specific production rates of prodigiosin formation were determined using batch culture technique. Sucrose as carbon source and NH₄NO₃ as nitrogen source resulted in a specific production rate of 0.476 mg prodigiosin (g cell dry weight)⁻¹ h⁻¹. Prodigiosin formation and productivity was inversely correlated to growth rate when the bacterium was grown under carbon limitation on a defined medium in a chemostat culture. The maximum specific growth rate (μ_max) was 0.54 h⁻¹ and prodigiosin was formed in amounts over 1 mg l⁻¹ up to a growth rate (μ) of 0.3 h⁻¹ at steady state conditions. At a dilution rate of 0.1 h⁻¹ growth at steady state with carbon and phosphate limitation supported prodigiosin formation giving a similar specific yield [1.17 mg prodigiosin (g cell dry weight)⁻¹ and 0.94 mg g⁻¹, respectively], however, cells grown with nitrogen limitation [(NH₄)₂SO₄] did not form prodigiosin. Productivity in batch culture was 1.33 mg l⁻¹ h⁻¹ as compared to 0.57 mg l⁻¹ h⁻¹ in the chemostat.     

The influence of the culture pH value on the direct glucose oxidative pathway in Klebsiella pneumoniae NCTC 418

Klebsiella pneumoniae NCTC 418 was cultured aerobically in chemostat cultures (D=0.3 h^-1; 35°C) under respectively carbon-, phosphate-, potassium-, sulphate-, and ammonia-limited conditions with glucose as the sole carbon and energy source. The effect of the external pH value on glucose metabolism and on the enzymes of the direct glucose oxidative pathway was examined. The pH value of the medium had a profound influence on both the activity and the synthesis of the glucose dehydrogenase and the gluconate dehydrogenase. At pH values ranging from pH 5.5 to pH 6.0 maximal activity and synthesis of these enzymes resulted in a more than 80% conversion of the glucose consumed into gluconate and 2-ketogluconate under potassium-or phosphate-limited conditions. On the other hand, no gluconate and/or 2-ketogluconate production could be detected when K. pneumoniae was cultured at pH 8.0. Whereas the synthesis of gluconate dehydrogenase seemingly was completely repressed, still some glucose dehydrogenase was present. The lack of glucose dehydrogenase activity at pH 8.0 was shown not to be due to the dissociation of the cofactor PQQ from the enzyme.Abbreviations DCIP dichlorophenol indophenol - PQQ pyrroloquinoline quinone [2,7,9-tricarboxy-1H-pyrrolo (2,3-f) quinoline-4,5-dione] - WB Wurster's Blue [1,4-bis-(dimethylamino)-benzene perchlorate]     

Heterotrophic growth of Thiobacillus acidophilus in batch and chemostat cultures

Heterotrophic growth of the facultatively chemolithoautotrophic acidophile Thiobacillus acidophilus was studied in batch cultures and in carbon-limited chemostat cultures. The spectrum of carbon sources supporting heterotrophic growth in batch cultures was limited to a number of sugars and some other simple organic compounds. In addition to ammonium salts and urea, a number of amino acids could be used as nitrogen sources. Pyruvate served as a sole source of carbon and energy in chemostat cultures, but not in batch cultures. Apparently the low residual concentrations in the steady-state chemostat cultures prevented substrate inhibition that already was observed at 150 M pyruvate. Molar growth yields of T. acidophilus in heterotrophic chemostat cultures were low. The Y _max and maintenance coefficient of T. acidophilus grown under glucose limitation were 69 g biomass · mol^–1 and 0.10 mmol · g^–1 · h^–1, respectively. Neither the Y _max nor the maintenance coefficient of glucose-limited chemostat cultures changed when the culture pH was increased from 3.0 to 4.3. This indicates that in T. acidophilus the maintenance of a large pH gradient is not a major energy-requiring process. Significant activities of ribulose-1,5-bisphosphate carboxylase were retained during heterotrophic growth on a variety of carbon sources, even under conditions of substrate excess. Also thiosulphate- and tetrathionate-oxidising activities were expressed under heterotrophic growth conditions.     

Optimization of exopolysaccharide production from Armillaria mellea in submerged cultures

Aims: To study the optimization of submerged culture conditions for exopolysaccharide (EPS) production by Armillaria mellea in shake‐flask cultures and also to evaluate the performance of an optimized culture medium in a 5‐l stirred tank fermenter. Methods and Results: Shake flask cultures for EPS optimal nutritional production contained having the following composition (in g l^?1): glucose 40, yeast extract 3, KH₂PO₄ 4 and MgSO₄ 2 at an optimal temperature of 22°C and an initial of pH 4·0. The optimal culture medium was then cultivated in a 5‐l stirred tank fermenter at 1 vvm (volume of aeration per volume of bioreactor per min) aeration rate, 150 rev min^?1 agitation speed, controlled pH 4·0 and 22°C. In the optimal culture medium, the maximum EPS production in a 5‐l stirred tank fermenter was 588 mg l^?1, c. twice as great as that in the basal medium. The maximum productivity for EPS (Q_p) and product yield (Y_P/S) were 42·02 mg l^?1 d^?1 and 26·89 mg g^?1, respectively. Conclusions: The optimal culture conditions we proposed in this study enhanced the EPS production of A. mellea from submerged cultures. Significance and Impact of the Study: The optimal culturing conditions we have found will be a suitable starting point for a scale‐up of the fermentation process, helping to develop the production of related medicines and health foods from A. mellea.     

Glucoamylase production in batch, chemostat and fed-batch cultivations by an industrial strain of Aspergillus niger

The Aspergillus niger strain BO-1 was grown in batch, continuous (chemostat) and fed-batch cultivations in order to study the production of the extracellular enzyme glucoamylase under different growth conditions. In the pH range 2.5–6.0, the specific glucoamylase productivity and the specific growth rate of the fungus were independent of pH when grown in batch cultivations. The specific glucoamylase producivity increased linearly with the specific growth rate in the range 0–0.1 h⁻¹ and was constant in the range 0.1–0.2 h⁻¹. Maltose and maltodextrin were non-inducing carbon sources compared to glucose, and the maximum specific growth rate was 0.19 ± 0.02 h⁻¹ irrespective of whether glucose or maltose was the carbon source. In fed-batch cultivations, glucoamylase titres of up to 6.5 g l⁻¹ were obtained even though the strain contained only one copy of the glaA gene. Received: 5 May 1999 / Received revision: 7 September 1999 / Accepted: 17 September 1999     

Influence of acetate on the growth of Candida utilis in continuous culture

Candida utilis was grown on acetate in chemostat cultures that were, successively, carbon and ammonia-limited (30° C; pH 5.5). With carbon(acetate)-limited cultures, the specific rate of oxygen consumption (q _{O 2}) was not a linear function of the growth rate but was markedly stimulated at the higher dilution rates, thus effecting a marked decrease in the Y _O value. This increased respiration rate, and decreased yield value, correlated closely with a marked increase in the extracellular acetate concentration. Under ammonia-limiting conditions, very low Y _O values were found, generally comparable with those found with carbon-limited cultures growing at the higher dilution rates, but these varied markedly with the extracellular acetate concentration. Thus, when the unused acetate concentration was raised progressively from about 5 g/l to about 21 g/l, the Y _O value decreased non-linearly from 11.4 to 5.8. When the extracellular acetate concentration was further increased to 25 g/l, growth was inhibited and the culture washed out. This relationship between respiration rate and the extracellular concentration of unused acetate was also markedly influenced by the culture pH value. Thus, with a fixed extracellular acetate concentration (16±2g/l) and dilution rate (0.14 h^–1), lowering the culture pH value progressively from 6.9 to 5.1 effected a marked and progressive increase in the respiration rate. Further lowering of the culture pH to 4.8, however, caused a complete collapse of respiration. In contrast to this situation, progressively lowering the pH value of an acetatelimited culture from 6.9 to 4.5 affected only slightly the culture respiration rate, and growth was possible even at a pH value of 2.5. These results are discussed in the context of the possible mechanisms whereby acetate exerts its toxic effect on the growth of C. utilis.