Organic acids and penicillin production

Summary Fed-batch fermentations with Penicillium chrysogenum, strain S 3723, were fed with glucose as carbon source or with a mixture of glucose and an organic acid (citrate, lactate, propionate, succinate, formate, or caproate). Increased yields of penicillin-V were observed with, propionate, and formate, 50% higher than in fermentations without acid in the feed. The yield with succinate was improved to the level previously observed with acetate (25%).     

Propionic acid fermentation by Propionibacterium acidipropionici: effect of growth substrate

Summary Batch propionic acid fermentations by Propionibacterium acidipropionici with lactose, glucose, and lactate as the carbon source were studied. In addition to propionic acid, acetic acid, succinic acid and CO₂ were also formed from lactose or glucose. However, succinic acid was not produced in a significant amount when lactate was the growth substrate. Compared to fermentations with lactose or glucose at the same pH, lactate gave a higher propionic acid yield, lower cell yield, and lower specific growth rate. The specific fermentation or propionic acid production rate from lactate was, however, higher than that from lactose. Since about equimolar acid products would be formed from lactate, the reactor pH remained relatively unchanged throughout the fermentation and would be easier to control when lactate was the growth substrate. Therefore, lactate would be a preferred substrate over lactose and glucose for propionic acid production using continuous, immobilized cell bioreactors. Correspondence to: S. T. Yang     

Kinetics of Bifidobacterium longum ATCC 15707 fermentations: effect of the dilution rate and carbon source

The effect of the dilution rate on biomass and product synthesis in fermentations of glucose, fructose and a commercial mixture of fructooligosaccharides (FOS) by Bifidobacterium longum ATCC 15707 was studied. Kinetic parameters (maximum specific growth rate, Monod constant, maintenance, and yield coefficients) in the mathematical model of the fermentation were estimated from experimental data. In the FOS mixture fermentations, approximately 12% of the total reducing sugars (mainly fructose) in the feed were not metabolized by the bacterium. In fermentations of fructose and the FOS mixture, biomass concentration increased as the dilution rate increased and, once maximum values were reached [3.90 (D=0.20 h^–1) and 2.54 g l^–1 (D=0.15 h^–1), respectively], decreased rapidly as the culture was washed out. Formic acid was detected at low dilution rates in glucose and fructose fermentations. The main products in fermentations of the three carbon sources were lactic and acetic acids. Average values of the molar ratio between acetic and lactic acids of 1.18, 1.21 and 0.83 mol mol^–1 were obtained in glucose, fructose and FOS mixture fermentations, respectively. In batch fermentations carried out without pH control this molar ratio was lower than 1.5 only when fructose was used as the carbon source.     

Measurement and analysis of intracellular ATP levels in metabolically engineered Zymomonas mobilis fermenting glucose and xylose mixtures

Intracellular adenosine-5'-triphosphate (ATP) levels were measured in a metabolically engineered Zymomonas mobilis over the course of batch fermentations of glucose and xylose mixtures. Fermentations were conducted over a range of pH (5-6) in the presence of varying initial amounts of acetic acid (0-8 g/L) using a 10% (w/v) total sugar concentration (glucose only, xylose only, or 5% glucose/5% xylose mixture). Over the design space investigated, ethanol process yields varied between 56.6% and 92.3% +/- 1.3% of theoretical, depending upon the test conditions. The large variation in process yields reflects the strong effect pH plays in modulating the inhibitory effect of acetic acid on fermentation performance. A corresponding effect was observed on maximum cellular specific growth rates, with the rates varying between a low of 0.15 h(-1) observed at pH 5 in the presence of 8 g/L acetic acid to a high of 0.32 +/- 0.02 h(-1) obtained at pH 5 or 6 when no acetic acid was initially present. While substantial differences were observed in intracellular specific ATP concentration profiles depending upon fermentation conditions, maximum intracellular ATP accumulation levels varied within a relatively narrow range (1.5-3.8 mg ATP/g dry cell mass). Xylose fermentations produced and accumulated ATP at much slower rates than mixed sugar fermentations (5% glucose, 5% xylose), and the ATP production and accumulation rates in the mixed sugar fermentations were slightly slower than in glucose fermentations. Results demonstrate that higher levels of acetic acid delay the onset and influence the extent of intracellular ATP accumulation. ATP production and accumulation rates were most sensitive to acetic acid at lower values of pH.     

Penicillin production by glucose-derepressed mutants ofPenicillium chrysogenum

Summary Wild-type strains ofPenicillium chrysogenum produce lower penicillin V titers in media containing excess glucose. Two mutant strains were isolated and shown to produce normal penicillin V titers in the presence of excess glucose. These strains, designated as glucose-repression insensitive (GRI) mutants, produced higher penicillin V titers than the wild-type strain in media containing lactose as the main carbohydrate source. In lactose-based media, the production of penicillin V was depressed to a much lesser extent by in-cycle additions of glucose with the GRI mutants when compared to the wild-type strain. In short-term biosynthesis experiments using washed cells in a medium containing glucose as the sole carbon source, the GRI mutants produced penicillin V at a faster rate than the wild-type strain. In fed-batch fermentations in 14-liter fermentors, where glucose was fed continuously and pH controlled, both GRI mutants produced more than 10% higher penicillin V titers than the wild-type strain. These results suggest that isolation of GRI mutants is an effective way to select for higher producing strains and that the synthesis of penicillin synthesizing enzymes in GRI mutants may be less repressed by glucose than in wild-type strains.     

Production of acetic acid by Dekkera/Brettanomyces yeasts under conditions of constant pH

Sixty yeast strains were previously screened for their ability to produce acetic acid, in shaken flask batch culture, from either glucose or ethanol. Seven of the strains belonging to the Brettanomyces and Dekkera genera, from the ARS Culture Collection, Peoria, IL, were further evaluated for acetic acid production in bioreactor batch culture at 28 °C, constant aeration (0.75 v/v/m) and pH (6.5). The medium contained either 100 g glucose/l or 35 g ethanol/l as the carbon/energy source. Dekkera intermedia NRRL YB-4553 produced 42.8 and 14.9 g acetic acid/l from the two carbon sources, respectively, after 64.5 h. The optimal pH was determined to be 5.5. When the initial glucose concentration was 150 or 200 g/l, the yeast produced 57.5 and 65.1 g acetic acid/l, respectively.     

Fed-batch fermentation with and without on-line extraction for propionic and acetic acid production byPropionibacterium acidipropionici

Fed-batch propionic and acetic acid fermentations were performed in semi-defined laboratory medium and in corn steep liquor withPropionibacterium acidipropionici strain P9. On average, over four experiments, 34.5 g/l propionic acid and 12.8 g/l acetic acid were obtained in about 146 h in laboratory medium with 79 g/l glucose added over five feeding periods. The highest concentration of propionic acid, 45 g/l, was obtained when the glucose concentration was not allowed to drop to zero. In corn steep liquor 35 g/l propionic acid and 11 g/l acetic acid were produced in 108 h from 59.4 g/l total lactic acid provided as seven feedings of corn steep liquor. Extractive fed-batch fermentations were conducted in semi-defined medium using either flat-sheet-supported liquid membranes or hollow-fiber membrane extraction to remove organic acids from the culture medium. As operated during the course of the fermentation, these systems extracted 25% and 22% of the acetic acid and 36.5% and 44.5% of the propionic acid, respectively, produced in the fermentation. Total amounts of acids produced were about the same as in comparable nonextractive fermentations: 30–37 g/l propionic acid and 13 g/l acetic acid were produced in 150 h. Limitations on acid production can be attributed to limited substrate feed, not to failure of the extraction system.Journal paper J-16303 of the Iowa Agriculture and Home Economics Experiment Station, Ames, Iowa. Project 3122.     

Production of acetic acid by Clostridium thermoaceticum in batch and continuous fermentations

Batch and continuous fermentations with Clostridium thermoaceticum (ATCC 39073) using automatic pH control were conducted. The value of mu(max) obtained from batch fermentation was about 0.14 h(-1); acetate yield, which was both growth and non-growth associated, was about 2 mole of acetic acid/mole of glucose, compared with a theoretical maximum value of 3. This low yield, compared with literature data, may be explained by glucose loss through a combination of degradation routes. Continuous fermentation could be sustained for 1600 h or more without contamination problems. Continuous fermentation at high dilution rates indicates that mu(max) may be well above 0.17 h(-1) when fresh feed medium is used. Acetate yields in continuous fermentation were about 77% of theoretical or 2.3 mole of acetic acid/mole of glucose.     

Production of carboxylic acids from hydrolyzed corn meal by immobilized cell fermentation in a fibrous-bed bioreactor

Corn meal hydrolyzed with amylases was used as the carbon source for producing acetic, propionic, and butyric acids via anaerobic fermentations. In this study, corn meal, containing 75% (w/w) starch, 20% (w/w) fibers, and 1.5% (w/w) protein, was first hydrolyzed using amylases at 60 degrees C. The hydrolysis yielded approximately 100% recovery of starch converted to glucose and 17.9% recovery of protein. The resulting corn meal hydrolyzate was then used, after sterilization, for fermentation studies. A co-culture of Lactococcus lactis and Clostridium formicoaceticum was used to produce acetic acid from glucose. Propionibacterium acidipropionici was used for propionic acid fermentation, and Clostridium tyrobutylicum was used for butyric acid production. These cells were immobilized on a spirally wound fibrous matrix packed in a fibrous-bed bioreactor (FBB) developed for multi-phase biological reactions or fermentation. The bioreactor was connected to a stirred-tank fermentor that provided pH and temperature controls via medium circulation. The fermentation system was operated at the recycle batch mode. Temperature and pH were controlled at 37 degrees C and 7.6, respectively, for acetic acid fermentation, 32 degrees C and 6.0, respectively, for propionic acid fermentation, and 37 degrees C and 6.0, respectively, for butyric acid production. The fermentation demonstrated a yield of approximately 100% and a volumetric productivity of approximately 1 g/(1 h) for acetic acid production. The propionic acid fermentation achieved an approximately 60% yield and a productivity of 2.12 g/(1 h), whereas the butyric acid fermentation obtained an approximately 50% yield and a productivity of 6.78 g/(1 h). These results were comparable to, or better than those fermentations using chemically defined media containing glucose as the substrate, suggesting that these carboxylic acids can be efficiently produced from direct fermentation of corn meal hydrolyzate. The corn fiber present as suspended solids in the corn meal hydrolyzate did not cause operating problem to the immobilized cell bioreactor as is usually encountered by conventional immobilized cell bioreactor systems. It is concluded that the FBB technology is suitable for producing value-added biochemicals directly from agricultural residues or commodities such as corn meal.     

The use of acetic acid as a source of carbon by cultured Chondrus crispus (Gigartinales,Rhodophyta) stackhouse

When growing seaweeds in tanks, pH and carbon source supply have to be controlled in order to maximize photosynthesis. pH can be controlled either by adding various inorganic acids which requires the extra addition of carbon, or by combining pH control and carbon source with for instance CO₂ or an organic acid such as acetic acid (CH₃COOH). We have found comparable productivity of Chondrus using CO₂ or CH₃COOH in tank culture with an increase in production of 25.0 and 27.5%, respectively, over the control. Laboratory experiments showed that acetic acid enabled us to maintain a steady state total inorganic carbon in the medium, the algae displaying an active photosynthesis. Experiments using labelled acetic acid CH₃-¹⁴COOH showed that the acid molecule or at least the -¹⁴COOH group is taken up by Chondrus although the mechanism was not elucidated. Preliminary extractions with hot ethanol showed that 67.9% of the label was solubilized from labelled tissue. Few counts were found in the carrageenans (< 1 %) and between 25.6 and 45.1% were found in the cellulosic residues. Acetic acid is suggested as an interesting means of regulating the pH and adding carbon in macrophyte culture.     

Optimization of Escherichia coli growth by controlled addition of glucose

During aerobic growth of Escherichia coli (recombinant K-12 and strain B) on protein hydrolysate (L-broth) and a carbon source (glucose), acetic acid is produced via glucose metabolism until the late log phase. At this point, the culture pH starts to increase and the growth rate decreases. In cultures without further glucose supplementation, these changes are associated with the accumulation of ammonia, the utilization of acetic acid, the depletion of amino acids, and the complete depletion of glucose. We hypothesize that, after depletion of the glucose, the bacteria catabolize amino acids for energy and carbon and give off the nitrogen as ammonia. Also contributing to the overall increase in pH is the depletion of the acetic acid produced earlier as it is metabolized upon exhaustion of glucose. However, there is a lag time of about 1 hour after the initial pH increase before the sustained accumulation of ammonia begins. This lag indicates that an unidentified factor, in addition to the increase in ammonia, contributes to the increase in pH. Advantage was taken of the turnaround from acid production to base production as reflected in the culture pH to implement the addition of glucose. In growth experiments during which the pH was controlled in the basic direction by glucose addition, the observed decrease in growth rate was significantly postponed and the pH change in the basic direction was reversed as a result of acid production by the cells from the newly added glucose. Furthermore, coll densities of twice that obtained without glucose feeding were demonstrated. Based on the media cost per unit cell density, the data indicate a 31% cost savings.     

Production of recombinant human growth hormone in Escherichia coli: expression of different precursors and physiological effects of glucose, acetate, and salts

The constitutive cytoplasmic expression in E. coli of human growth hormone (hGH) with different N-terminal extensions (3 or 4 amino acids) has been studied. These hGH precursors were used for in vitro cleavage to obtain the mature, authentic hormone. Small changes in the amino acid extensions of the hGH precursors led to three-fold differences in specific expression rates. The specific expression rate of the hGH precursors was inversely proportional to the ratios of the specific growth rates of plasmid containing and plasmid free cells (micro(+)/micro(-)) and also to the genetic stability. To ensure a satisfactory genetic stability in production fermentors, an hGH precursor with a moderate expression efficiency was chosen.The medium composition and growth conditions were studied, resulting in the choice of a glucose fed batch fermentation process using a complex medium. In this process a yield of 2000 mg/L of met-ala-glu-hGH (MAE-hGH) was obtained. The fermentation process comprised a glucose-limited growth phase followed by a second phase with increased glucose feed and exhaustion of phosphate from the medium. The second phase is characterized by an MAE-hGH production, whereas further biomass formation is blocked. High concentrations of glucose led to reduced specific expression of MAE-hGH--the specific and total yield in batch glucose fermentations is only about 30% of the yield in optimized fed batch fermentations. The physiological background for this was investigated. Chemostat experiments showed that the glucose concentration and the metabolic condition of the cells--i.e. with or without formation of acetate--was not critical per se in order to obtain a high specific yield of MAE-hGH. Therefore it is unlikely that formation of MAE-hGH is catabolite repressed by glucose. Furthermore it was shown that the specific production rate of MAE-hGH was independent of the specific growth rate and it was further demonstrated that the decrease in expression efficiency in glucose batch fermentation was a result of an inhibitory effect of acetic acid. In batch fermentations this inhibitory effect was enhanced by a salt effect caused by increased consumption of acid and base used to control pH. The identity of the acid and the base used are not important in this context. From studies of the expression of other proteins in E. coli. with constitutive as well as inducible promoters we conclude that glucose fed batch processes are often superior to batch processes in the production of heterologous proteins E. coli.     

Acid-base equilibrium in aerobic fermentations: influence of unutilizable acids and bases on acetic acid concentration in culture liquid

An investigation was made on the factors influencing the acetic acid concentration in the culture liquid of the aerobic fermentations where acetie acid was used as a carbon source. The acetic acid concentration in the culture liquid changed in proportion to the amount of unutilizable acid or base supplied. This was explained by the principle of conservation of electroneutrality. Another factor affecting the acetic acid concentration in the culture liquid was bicarbonate ions which were formed by the dissolution and dissociation of carbon dioxide in the gas phase of the fermentor. The increment in bicarbonate ion concentration was equal to the decrement in the acetie acid concentration in the culture liquid.     

Mannitol production by heterofermentative <Emphasis Type="BoldItalic">Lactobacillus reuteri</Emphasis> CRL 1101 and <Emphasis Type="BoldItalic">Lactobacillus fermentum</Emphasis> CRL 573 in free and controlled pH batch fermentations

Certain lactic acid bacteria, especially heterofermentative strains, are capable to produce mannitol under adequate culture conditions. In this study, mannitol production by Lactobacillus reuteri CRL 1101 and Lactobacillus fermentum CRL 573 in modified MRS medium containing a mixture of fructose and glucose in a 6.5:1.0 ratio was investigated during batch fermentations with free pH and constant pH 6.0 and 5.0. Mannitol production and yields were higher under constant pH conditions compared with fermentations with free pH, the increase being more pronounced in the case of the L. fermentum strain. Maximum mannitol production and yields from fructose for L. reuteri CRL 1101 (122 mM and 75.7 mol%, respectively) and L. fermentum CRL 573 (312 mM and 93.5 mol%, respectively) were found at pH 5.0. Interestingly, depending on the pH conditions, fructose was used only as an alternative external electron acceptor or as both electron acceptor and energy source in the case of the L. reuteri strain. In contrast, L. fermentum CRL 573 used fructose both as electron acceptor and carbon source simultaneously, independently of the pH value, which strongly affected mannitol production by this strain. Studies on the metabolism of these relevant mannitol-producing lactobacilli provide important knowledge to either produce mannitol to be used as food additive or to produce it in situ during fermented food production.     

Pulsed feeding during fed-batch fungal fermentation leads to reduced viscosity without detrimentally affecting protein expression

The goal in this study was to determine if pulsed addition of substrate could be used to alter filamentous fungal morphology during fermentation, to result in reduced broth viscosity. In all experiments, an industrially relevant strain of Aspergillus oryzae was grown in 20-liter fermentors. As a control, cultures were fed limiting substrate (glucose) continuously. Tests were performed by altering the feeding strategy so that the same total amount of glucose was fed in repeated 300-s cycles, with the feed pump on for either 30 or 150 s during each cycle. Variables indicative of cellular metabolic activity (biomass concentration, oxygen uptake rate, base consumed for pH control) showed no significant difference between continuous and pulse-fed fermentations. In addition, there was no significant difference between total extracellular protein expression or the apparent distribution of these proteins. In contrast, fungal mycelia during the second half of pulse-fed fermentations were approximately half the size (average projected area) of fungi during fermentations with continuous addition of glucose. As a result, broth viscosity during the second half of pulse-fed fermentations was approximately half that during the second half of continuous fermentations. If these results prove to be applicable for other fungal strains and processes, then this method will represent a simple and inexpensive means to reduce viscosity during filamentous fungal fermentation.     

Production of a novel bioflocculant by fed-batch culture of Citrobacter sp.

Production of a novel bioflocculant by a fed-batch culture of Citrobacter sp. TKF04 was investigated using acetic acid as a sole carbon source. Synthesis of the bioflocculant was favored by dissolved O₂ tension at 20% of air saturation and C/N ratio (mol acetic acid/mol ammonium) of 10:1 in the feed solution. Under optimal conditions, 4.6 g crude bioflocculant per liter broth was produced, whose flocculating activity was 22 300 units. This activity was 9 times higher than that of the control (only acetic acid was supplied).     

Production of butanol by Clostridium puniceum in batch and continuous culture

Summary The pink-pigmented, amylolytic and pectinolytic bacterium Clostridium puniceum in anaerobic batch culture at pH 5.5 and 25–30°C produced butan-1-ol as the major product of fermentation of glucose or starch. The alcohol was formed throughout the exponential phase of growth and surprisingly little acetone was simultaneously produced. Furthermore, acetic and butyric acids were only accumulated in low concentrations, and under optimal conditions were completely re-utilised before the fermentation ceased. Thus, in a minimal medium containing 4% w/v glucose as sole source of carbon and energy, after 65 h at 25°C, pH 5.5 all of the glucose had been consumed to yield (g product/100 g glucose utilised) butanol 32, acetone 3 and ethanol 2. Butanol was again the major product of glucose fermentation during phosphate-limited chemostat culture wherein, although the organism eventually lost its capacity to sporulate and to synthesize granulose, production of butanol continued for at least 100 volume changes. Under no growth condition was the organism capable of producing more than 13.3 g l^-1 of butanol. At pH 5.5, growth on pectin was slow and yielded a markedly lesser biomass concentration than when growth was on glucose or starch; acetic acid was the major fermentation product with lower concentrations of methanol, acetone, butanol and butyric acid. At pH 7, growth on all substrates produced virtually no solvents but high concentrations of both acetic and butyric acids.     

热带假丝酵母细胞内pH的测定及其与生长代谢活性的关系

应用荧光探针5(6)-双醋酸羧基荧光素 (Carboxyfluorescein diacetate) 测定了产长链二元酸热带假丝酵母 (Candida tropicalis) 细胞内pH (pHi) 值,确定了该探针载入C. tropicalis细胞的适宜条件。用摇瓶培养C. tropicalis细胞,考察了细胞外pH和生长碳源对pH_I的影响,实验结果表明：细胞外pH对pH_I略有影响,而生长碳源对pH_I的影响略为明显。利用5L发酵罐进一步研究了细胞生长代谢活性与pHi的关系,结果表明：细胞比生长速率、CO₂比生产速率和葡萄糖比消耗速率与pHi变化密切相关,pH_I的增加伴随着细胞生长活力的增加,反之亦然。在pH6.0条件下用葡萄糖和醋酸钠共作碳源培养C. tropicalis细胞时,测得的pH_I值维持在5.72～6.15范围内。     

Effects of ptb knockout on butyric acid fermentation by Clostridium tyrobutyricum

Clostridium tyrobutyricum ATCC 25755 is an anaerobic, rod-shaped, gram-positive bacterium that produces butyrate, acetate, hydrogen, and carbon dioxide from various saccharides, including glucose and xylose. Phosphotransbutyrylase (PTB) is a key enzyme in the butyric acid synthesis pathway. In this work, effects of ptb knockout by homologous recombination on metabolic flux and product distribution were investigated. When compared with the wild type, the activities of PTB and butyrate kinase in ptb knockout mutant decreased 76 and 42%, respectively; meanwhile, phosphotransacetylase and acetate kinase increased 7 and 29%, respectively. However, ptb knockout did not significantly reduce butyric acid production from glucose or xylose in batch fermentations. Instead, it increased acetic acid and hydrogen production 33.3-53.8% and ≈ 11%, respectively. Thus, the ptb knockout did increase the carbon flux toward acetate synthesis, resulting in a significant decrease (28-35% reduction) in the butyrate/acetate ratio in ptb mutant fermentations. In addition, the mutant displayed a higher specific growth rate (0.20 h(-1) vs. 0.15 h(-1) on glucose and 0.14 h(-1) vs. 0.10 h(-1) on xylose) and tolerance to butyric acid. Consequently, batch fermentation with the mutant gave higher fermentation rate and productivities (26-48% increase for butyrate, 81-100% increase for acetate, and 38-46% increase for hydrogen). This mutant thus can be used more efficiently than the parental strain in fermentations to produce butyrate, acetate, and hydrogen from glucose and xylose.     

Succinic acid production with reduced by-product formation in the fermentation of Anaerobiospirillum succiniciproducens using glycerol as a carbon source

Succinic acid was produced by fermentation of Anaerobiospirillum succiniciproducens using glycerol as a carbon source. When cells were anaerobically cultured in a medium containing 6.5 g/L glycerol, a high succinic acid yield (133%) was obtained while avoiding the formation of by-product acetic acid. The gram ratio of succinic acid to acetic acid was 25.8:1, which is 6.5 times higher than that obtained using glucose (ca. 4:1) as a carbon source. Therefore, succinic acid can be produced with much less by-product formation by using glycerol as a carbon source, which will facilitate its purification. When glucose and glycerol were cofermented with the increasing ratio of glucose to glycerol, the gram ratio of succinic acid to acetic acid and succinic acid yield decreased, suggesting that glucose enhanced acetic acid formation irrespective of the presence of glycerol. Glycerol consumption by A. succiniciproducens required unidentified nutritional components present in yeast extract. By intermittently feeding yeast extract along with glycerol, a high succinic acid yield (160%) could be obtained while still avoiding acetic acid formation. This resulted in the highest ratio of succinic acid to acetic acid (31.7:1).