Production of biosurfactants by the resting cells ofPseudomonas aeruginosa CFTR-6

A resting cell system was used for the production of glycolipids byPseudomonas aeruginosa CFTR-6. In this, the growth phase was separated from the production phase to overcome the inhibition of glycolipid production by inorganic phosphate. It was shown that when the cells were transferred after the growth phase into a medium devoid of phosphate, glycolipid production was increased nearly twofold. The maximum glycolipid concentration was attained much more rapidly than the conventional batch fermentation system, thus increasing the productivity.     

Nicotine production by “hairy root” cultures of Nicotiana rustica: Fermentation and product recovery

The production of nicotine by cultures ofNicotiana rustica transformed withAgrobacterium rhizogenes has been examined in a packed bed fermenter as a two-stage batch/continuous-flow system. A substantial proportion of the nicotine synthesised in the batch phase may be subsequently harvested from the medium. The possibility of improving product recovery using macroreticular adsorbents is considered.     

Phosphate effects in the fermentation of α-amylase by Bacillus amyloliquefaciens

Summary The effects of phosphate on -amylase fermentation byBacillus amyloliquefaciens were investigated. It was observed through batch culture that optimal phosphate level which maximizes -amylase biosynthesis exists. High concentration of phosphate level promotes maltose uptake and growth of the microorganism, while high maltose uptake rate in the microorganism at the same time represses the enzyme biosynthesis presumably due to catabolite repression inside the microorganism. In continuous cultivation, a steady state of -amylase biosynthesis was obtained by maintaining phosphate level at a certain level. In fed-batch culture, by intermittant feeding of phosphate as well as maltose, higher activity of -amylase in the broth was obtained compared to the result from single nutrient feeding.     

Improved algal oil production from Botryococcus braunii by feeding nitrate and phosphate in an airlift bioreactor

To improve biomass and microalgal oil production of Botryococcus braunii, fed‐batch culture was investigated in an airlift photobioreactor. The optimal feeding time of the fed‐batch culture was after 15 days of cultivation, where 1.82 g/L of the microalgal biomass was obtained in the batch culture. Nitrate nutrient was the restrictive factor for the fed‐batch cultivation while phosphate nutrient with high concentration did not affect the microalgal growth. The optimal mole ratio of nitrate to phosphate was 34.7:1, where nitrate concentration reached the initial level and phosphate concentration was one quarter of its initial level. With one feeding, the biomass of B. braunii reached 2.56 g/L after 18 days. Two feedings in 2‐day interval enhanced the biomass production up to 2.87 g/L after 19 days of cultivation. The hydrocarbon content in dry biomass of B. braunii kept at high level of 64.3% w/w. Compared with the batch culture, biomass production and hydrocarbon productivity of B. braunii were greatly improved by the strategic fed‐batch cultivation.     

Evaluation of the SCP from Opuntia juice

Summary In deseeded opuntia juice medium batch and continuous cultivation ofCandida utilis produced 12 and 19.9gl^–1 yield of the SCP respectively. Its biological value(72), digestibility coefficient(70) and protein score(58) indicated it to be a good protein.     

Stability of plasmid PBR322 in Escherichia coli immobilized on cotton cloth during use as resident inoculum

Summary E. coli cells harbouring plasmid pBR322 which confers ampicillin resistance were immobilized on cotton cloth. The resulting film was used as an inoculum in daily repeated batch culture in ampicillin-free medium. During two months, the film was able to produce cultures which, at the late log phase, showed little sensitivity to 10 mg/ml ampicillin. Thus such a bacterial film can effectively be used as an inoculum for the production of recombinant DNA products by means of pBR322 or its derivatives in the absence of ampicillin.     

Enhanced cellulase production using Solka Floc in a fed-batch fermentation

Summary Use of a fed-batch mode of cultivation of T. reesei has permitted high concentrations of substrate to be consumed. This has resulted in the production of high titre cellulase preparations around 30 FPU/ml at high volumetric productivities (177 IU/L.hr).Perhaps the most obvious area for major improvement in the process of cellulose utilization is the production of cellulase enzyme for hydrolysis of wood and agricultural residues. It has been estimated that some 50% of the cost of producing glucose from cellulosic material is attributable to enzyme production alone (Perez, et al., 1980). Improvements in the area would therefore have a dramatic impact, and are of paramount importance if economical hydrolysis processes are to be realized. The first major thrust in the area has been the development of improved mutant strains of T. reesei, free from catabolite repression and capable of constitutive cellulase production (Montenecourt and Eveleigh, 1977; Gallo, 1982).While this effort continues to develop further high yielding mutants, improvement must also come from developments in fermentation techniques. A major advance is the use of fed-batch cultivation, which provides a means of avoiding the agitation and aeration difficulties, as well as repression effects encountered with high substrate concentration batch fermentation. This report briefly compares batch and fed-batch operation over a range of substrate concentrations.     

Growth ofEscherichia coli B in a continuous culture under limitation by inorganic phosphate

During batch cultivation ofEscherichia coli in a medium deficient in inorganic phosphate, the growth curve after exhaustion of phosphate is linear. Results obtained in batch cultivation were used for deriving expressions for bacterial growth at a constant rate in a single-and multi-stage continuous system. It was found experimentally that the theoretical relations derived are satisfactory.     

Fed-batch fermentation of glucose to acetate by an improved strain ofClostridium thermoaceticum

The fed-batch approach to the production of acetate from glucose by an improved strain ofClostridium thermoaceticum resulted in better performance than the batch fermentation, especially in media containing an excess (3X) of nutrients and trace salts. At pH 6.6, 46 g/l acetic acid was produced in 192 hours with 93% substrate utilization. In contrast, batch fermentation under similar conditions resulted in a maximum of 35 g/l acetic acid with less than 82% substrate utilization.     

Quantitative characterization of plasmid instability inSaccharomyces cerevisiae using flow cytometry-cell sorting

Summary The fraction of daughter cells ofS. cerevisiae YT76 born without plasmids increases significantly during the postexponential phase of batch growth. Plasmid segregation data presented is obtained using a new method based on rapid flow cytometry-cell sorting isolation of subpopulations consisting of newborn daughter cells and dividing mother cells.     

Cell proliferation-cephamycin biosynthesis relationship in the culture of Streptomyces lactamdurans L 2/6: phosphate regulation

During batch cultivation of Streptomyces lactamdurans a diauxic growth has been shown taking into consideration dry cell mass, protein, and DNA determination. This phenomenon was connected with substantial changes in environmental conditions such as concentrations of ammonia and amino nitrogen, soluble inorganic phosphate and pH. The antibiotic production was preceded by the preparatory phase occurring at the beginning of the second growth phase. A hypothetical pattern of cell physiology in the curse of cephamycin fermentation is discussed. An essential part in the biphasic cell growth and the induction of antibiotic synthesis in this model is played by phosphate depletion in the medium.     

Production of acetic acid in packed bed fermenters

Summary Production of acetic acid from ethanol byAcetobacter aceti attached to a variety of support materials has been examined in fixed-film packed bed fermenters. Overall batch acid productivities with triangular ceramic particles and nylon mesh were respectively 56% and 30% greater than that for woodshavings, with comparable high acid yields. The highest batch acid productivity attained was 0.75 g/l h with the ceramic support. Continuous operation with the same material resulted in an acid productivity of 4.0 to 4.5 g/l h at a yield of 80%. This was increased to 10.7 g/l h by feeding oxygen-enriched air to the fermenter.Stability of theAcetobacter populations, judged by reproducibility in batch operation and attainment, reproducibility and maintenance of steady operating conditions in continuous operation, was very high.     

Development of media for growth ofDioscorea Deltoidea cells andin vitro diosgenin production: Influence of media constituents and nutrient stress

Summary Callus culture ofDioscorea deltoidea produced diosgenin and sterols during stationary phase. Ammonium nitrate (420 mg Nitrogen/l) as sole nitrogen source supported better growth than a combination of ammonium nitrate and potassium nitrate (totally equivalent to 840 mg Nitrogen/l). The production of diosgenin increased under low phosphate concentration (100 mg/l) whereas high phosphate concentration (240 mg/l) promoted growth. Micronutrients, when used at 1 1/2 strength, enhanced growth and diosgenin production. Depletion of nitrogen increased the diosgenin synthesis by a factor of 2. Adoption of a two stage culture method enhanced the diosgenin production in cultured cells by eight-fold.     

Regulation of phosphate metabolism during intracellular lipid production inRhodotorula gracilis

Summary ³¹P NMR spectra of intact cells ofRhodotorula gracilis showed pH dependent inorganic phosphate (P_i) signals from two different compartments, namely, vacuole and cytoplasm. Clear distinction between growth phase and lipid accumulation phase was inferred by monitoring glycerol 3-phosphate and polyphosphate signals. The role of glycerol 3-phosphate in lipid production and the significance of polyphosphate accumulation during the same is discussed.     

Biosensor online control of citric acid production from glucose by Yarrowia lipolytica using semicontinuous fermentation

Our study aimed at the development of an effective method for citric acid production from glucose by use of the yeast Yarrowia lipolytica. The new method included an automated bioprocess control using a glucose biosensor. Several fermentation methodologies including batch, fed‐batch, repeated batch and repeated fed‐batch cultivation were tested. The best results were achieved during repeated fed‐batch cultivation: Within 3 days of cycle duration, approximately 100 g/L citric acid were produced. The yields reached values between 0.51 and 0.65 g/g and the selectivity of the bioprocess for citric acid was as high as 94%. Due to the elongation of the production phase of the bioprocess with growth‐decoupled citric acid production, and by operating the fermentation in cycles, an increase in citric acid production of 32% was achieved compared with simple batch fermentation.     

A novel one step process for cellulose fermentation using mesophilic cellulolytic and glycolytic Clostridia

Summary A mesophilic cellulolytic Clostridium has been isolated and coculture of this Clostridium and Clostridium acetobutylicum was established. In 9 days, 7 g/l of Solka Floc were fermented by the monculture. During the same time of incubation, 20 g/l of Solka Floc were degraded by the coculture, and 27 g/l in 8 days in a fed batch fermentation. Only the first phase of the acetone butanol fermentation (acid formation) was observed.     

Aerobic glucose metabolism of Saccharomyces kluyveri: growth, metabolite production, and quantification of metabolic fluxes.

The growth and product formation of Saccharomyces kluyveri was characterized in aerobic batch cultivation on glucose. At these conditions it was found that ethyl acetate was a major overflow metabolite in S. kluyveri. During the exponential-growth phase on glucose ethyl acetate was produced at a constant specific rate of 0.12 g ethyl acetate per g dry weight per hour. The aerobic glucose metabolism in S. kluyveri was found to be less fermentative than in S. cerevisiae, as illustrated by the comparably low yield of ethanol on glucose (0.08 +/- 0.02 g/g), and high yield of biomass on glucose (0.29 +/- 0.01 g/g). The glucose metabolism of S. kluyveri was further characterized by the new and powerful techniques of metabolic network analysis. Flux distributions in the central carbon metabolism were estimated for respiro-fermentative growth in aerobic batch cultivation on glucose and respiratory growth in aerobic glucose-limited continuous cultivation. It was found that in S. kluyveri the flux into the pentose phosphate pathway was 18.8 mmole per 100 mmole glucose consumed during respiratory growth in aerobic glucose-limited continuous cultivation. Such a low flux into the pentose phosphate pathway cannot provide the cell with enough NADPH for biomass formation which is why the remaining NADPH will have to be provided by another pathway. During batch cultivation of S. kluyveri the tricarboxylic acid cycle was working as a cycle with a considerable flux, that is in sharp contrast to what has previously been observed in S. cerevisiae at the same growth conditions, where the tricarboxylic acid cycle operates as two branches. This indicates that the respiratory system was not significantly repressed in S. kluyveri during batch cultivation on glucose.     

Production of yeast SCP from corn stover hydrolysates

The relative ease with which the hemicellulose component present in agricultural residues are hydrolyzed makes these raw materials attractive sources of sugars for the production of SCP. Corn stover has been selected for this study as a representative of a wide variety of crop residues of potential interest. The hydrolysates obtained by treating this material with dilute acid solutions were supplemented with non-carbon nutrients and the mixture of pentoses and hexoses converted into yeast biomass by a strain of Candida utilis in submerged cultivation. To be economically attractive mild hydrolysis conditions were considered although incomplete hydrolysis to monosaccharides were obtained. The performance of the fermentation has been studied in batch as well as in continuous systems. High efficiency of substrate utilization and protein productivity were obtained with a special yeast strain (CMI-23311) compared to the one (ATCC-9226) commonly studied as SCP source.     

A mathematical model of growth and alkaloid production in the submerged culture of Claviceps purpurea

A mathematical model of the batch cultivation of Claviceps purpurea was formulated. The main attention was devoted to the effect of exocellular and intracellular phosphate on the growth of the mycelium and production of clavine alkaloid under experimental conditions without limitation by carbon and nitrogen sources. The method of nonlinear regression was used ot predict the optional technological regime of the phosphate addition in the batch culture at different time intervals of additions.     

CH4 production from H2 and CO2 byMethanobacterium thermoautotrophicum cells fixed on hollow fibers

Summary Methane was produced from H₂ and CO₂ byMethanobacterium thermoautotrophicum cells fixed on the surface of hollow fibers. The mineral solution permeated through the inside of fibers was consumed by the cells, while the gaseous substrate flowing outside the fibers was directly metabolized to methane. Methane production was proportional to hollow fiber length i.e., contact area between cell layer and gas phase. In repeated batch cultures, the production rates of methane and cell mass were 33.1 L/L reactor/day and 1.75 g cells/L reactor/day, respectively with 90% conversion rate.