Growth and cell wall composition of glucose-limited bean cells (Phaseolus vulgaris L.)

Glucose-limited bean cells (Phaseolus vulgaris L.) were grown in a modified bacterial fermentor at a constant pH of 4.8. The cultures were kept in steady state at different specific growth rates varying from 0.00216 h^–1 to 0.0106 h^–1. Culture conditions are described that are needed to start a continuous culture. First, it was essential to use log-phase cells as starting material. Second, it was important to increase the dilution rate gradually, otherwise cells in the culture aggregated. Cells grown at the highest dilution rate employed contained twice as much protein per gram dry weight as cells grown at the lowest dilution rate. The composition of the cell walls also varied with the dilution rate in contrast to their relatively constant composition when grown in batch culture.     

Storage in water ofRhizobium phaseoli cells harvested from continuous culture and its effect on biological nitrogen fixation

Summary Taken cells from cultures ofRhizobium phaseoli grown at different dilution rates were tested for plant growth promotion in a bioassay withPhaseolus vulgaris, before and after storage in water for one month. Cells grown at higher dilution rates showed a greater loss of effectiveness     

Morphological behaviour ofSaccharomyces cerevisiae during continuous fermentation

Summary Saccharomyces cerevisiae were observed to undergo drastic morphological changes when grown in continuous culture. Peak elongations and minimum cell volumes were found at intermediate dilution rates when it was believed the insitu glucose concentration was at its lowest. The shapes and sizes were reproducible and have been quantified at two different glucose feed concentrations.     

Production of ethanol by adsorbed yeast cells

Summary Various ion exchange resins were tested for their ability to adsorb cells of Saccharomyces cerivisiae with the ultimate intention of developing a packed bed immobilized cell reactor for the continuous production of ethanol. The resins varied greatly in their ability to adsorb cells - the least effective resins retained less than 1 mg S. cerivisiae cells (dry weight)/g of resin (dry weight), and the most effective, 130–140 mg cells/g of resin. A column reactor packed with adsorbed yeast cells was operated continuously for over 200 hours using a 12% (w/v) glucose medium at dilution rates of 1.1 h^-1 and 1.44 h^-1 (based on void volume). High ethanol productivities of 53.1 and 62.0 g ethanol/l-h were obtained.     

Acetone-butanol production by Clostridium acetobutylicum in an ammonium-limited chemostat at low pH values

Clostridium acetobutylicum was grown in continuous culture under ammonium limitation (15.15 mM NH₄ ⁺). At a pH of 6.0 and at various dilution rates only acetate, butyrate and ethanol were formed as non-gaseous products. A decrease of the pH to values between 5.2 and 4.3 resulted in a shift of the fermentation towards acetone-butanol formation.     

Enhanced plasmid maintenance in a CSTR upon square-wave oscillations in the dilution rate

Summary The effects of forced square-wave perturbations in the dilution rate on plasmid maintenance and gene expression of a population ofEscherichia coli K12 strain carrying the vector plasmid pBR322 grown in a chemostat with a non-selective medium were studied. It was observed that in the control experiments, where the dilution rates were kept constant, the percentage of plasmid-containing cells decreased after a period of time. Eventually, the culture was displaced by the plasmid-free cells. However, when the cells were exposed to forced oscillations in the dilution rate, the reactor culture was able to maintain a mixed population of plasmid-free and plasmid-containing cells for a longer period of time. The above observation seems to be independent of the source of the host cells. That is, the same results were obtained when the plasmid-free cells were generated from the culture itself due to defective partitioning of the plasmids or introduced externally.     

Growth of Dioscorea deltoidea at high sugar concentrations

Dioscorea deltoidea cell suspension cultures were grown at initial sucrose concentrations of 35 to 200 g/L. The growth rates were similar (about 0.50 day^–1) with all of the initial sugar concentrations examined. The ratio of fresh weight to dry weight of cells was dependent on the initial sugar concentration, however, it remained fairly constant as long as the sugar was present in the growth medium. These results are different from results recently published, claiming that the growth rate of D. deltoidea cells is dependent on sugar concentration and the fresh weight to dry weight ratio increases throughout growth.     

Cell yields and fermentation responses of a <Emphasis Type="Italic">Salmonella</Emphasis> Typhimurium poultry isolate at different dilution rates in an anaerobic steady state continuous culture

The objectives of these studies were to determine cell yield and fermentation responses of a Salmonella enterica serovar Typhimurium poultry isolate using various dilution rates in steady state continuous culture incubations. S. enterica Typhimurium cells were propagated in continuous cultures with a total volume of 0.50 l of Luria Bertani medium containing 0.1% glucose. Dilution rates from 0.0125 to 1.44/h were used. Cell protein concentration generally increased linearly with increased dilution rate up to a rate of 0.54/h and declined at the higher dilution rates. Glucose consumption gave a similar pattern to cell protein concentration by declining at the three highest dilution rates. Short chain fatty acid production was inconsistently influenced by dilution rate. Acetate, the most predominant fatty acid produced, declined at the higher dilution rates, as did propionate. Ammonia production remained stable at the lowest dilution rates, but increased significantly at a dilution rates above 0.27/h.     

Effects of organism type and growth conditions on cell disruption by impingement

Data for disruption of C. utilis, S. cerevisiae and B. subtilis cells by impingement of a high velocity jet of suspended cells against a stationary surface are compared. Differences between organisms were observed, but there were no general differences found between yeast and bacteria. In addition, growth conditions were found to have an effect on disruption with cells grown at a high specific growth rate easier to disrupt than cells grown at a low rate.Nomenclature a exponent of pressure (dimensionless) - D dilution rate (h^\s-1) - K dimensional rate constant (Pa ^\s-) - N number of passes (dimensionless) - P operating pressure (Pa) - R fraction of cells disrupted (dimensionless) - u_m maximum specific growth rate (h^\s-1)     

An automatic,on-line glucose analyzer for feed-back control of fed-batch growth of Escherichia coli

Summary A computer-assisted on-line glucose analyzer was developed for feed-back control of cell growth. Using this system the glucose consumption rate for Escherichia coli was determined to be linear during batch culture at 0.37 g/hr. On-line feed-back control of glucose concentration at 1.5±0.5 g/L was used with fed-batch cultures to produce 31.2 g dry weight of E. coli cells/L in 12 h.     

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 impeller speed upon the pullulan fermentation

Summary The effect of impeller speed on pullulan production and the morphology ofAureobasidium pullulans in batch culture was studied. Pullulan production and the percentage of yeast cells in the culture rose with impeller speed, as did molecular weight of the polysaccharide.     

A new method for quantifying the probability of segregative plasmid loss inEscherichia coli B/r

Summary A new method for quantifying rates of segregative plasmid loss is described. The probability of plasmid loss is found from the decrease in the fraction of plasmid containing cells, following a synchronous division. Stability inEscherichia coli B/r increased with pH and dilution rate, but decreased with temperature.     

Continuous high rate production of ethanol by Zymomonas mobilis in an attached film expanded bed fermentor

Summary Experiments were conducted with Zymomonas mobilis in an attached film expanded bed (AFEB) fermentor at different dilution rates, using a feed glucose concentration of 100 gm/l. Vermiculite was used as the bed material for attachment of the bacterial film. Ethanol volumetric productivities were maximum at a dilution rate of 3.6hr^-1. The productivities were 105 gm/l-hr and 210 gm/l-hr based on total fermentor volume and bed volume, respectively.     

Involvement of d-lactate and lactic acid racemase in the metabolism of glucose by Selenomonas ruminantium

Selenomonas ruminantium HD4 produced significant quantities of d- and l-lactate from glucose in batch culture. Both isomers also supported growth if fumarate was present. In glucose-limited continuous culture, d-lactate was detected in the medium only at fast dilution rates. In continuous-culture-grown cells, only a cytoplasmic NAD-dependent l-lactate dehydrogenase (LDH) and a membrane-associated NAD-independent l-LDH were detected; activity of the soluble enzyme was twice as high at the fast dilution rate as at the slow dilution rate. Lactate racemase was also detected; its activity was 4-fold higher at the fast dilution rate. The presence of racemase explains why d-lactate was made and used by this organism.     

Somatic cell genetic studies inBrassica species

In vitro culture ofBrassica alba anthers on a growth medium containing inorganics of KB5 and organics, iron, sucrose and hormones of B5 resulted in a very high response of anthers (93.75%) towards callus induction. All the calli transferred to regeneration media responded favourably even after six months of callus induction. Numerous torpedo-shaped embryoids developed in clusters at many sites from each callus mass. Secondary embryogenesis and multiple shoot formation was also observed in many cases. The number of embryoids and plantlets produced by one embryogenic anther were as high as 169.8 and 17 respectively. 87% of the regenerated plants were haploids.     

Conversion of cellobiose and xylose to ethanol by immobilized growing cells of Clostridium saccharolyticum on charcoal support

Summary An immobilization technique has been developed for the conversion of both cellobiose and xylose to ethanol, which may be considered as one stage of a process for the conversion of cellulosic biomass to ethanol. Relatively inexpensive charcoal was used as a support material, with 23 mg dry weight of Clostridium saccharolyticum cells per g dry weight of support. Tests were run for 170 h at 0.15 1/h dilution rate. From a 3% (w/v) sugar mixture, 0.7% (w/v) ethanol was obtained with over 97% cellobiose and 62% xylose utilization.     

Semi-continuous production of sanguinarine and dihydrosanguinarine by Papaver somniferum L. cell suspension cultures treated with fungal homogenate

Papaver somniferum L. (opium poppy) cells were elicited with a Botrytis sp. homogenate and cultured by a semi-continuous process. Elicitation induced synthesis of sanguinarine and dihydrosanguinarine. Significant release of both alkaloids into the culture medium occurred. Medium exchange at 2-day intervals enabled product recovery from spent medium and maintained culture viability. Culture growth was not inhibited by elicitor treatment necessitating sub-culture prior to re-elicitation. Re-elicited cultures displayed an increasing sensitivity (reduced growth rate, higher alkaloid yield) to the elicitor with each successive treatment and did not survive a fourth elicitation.Abbreviations DW dry weight - FW fresh weight - 2,4-D 2,4-dichlorophenoxyacetic acid - SGE sanguinarine - DSGE dihydrosanguinarine Publication 29143 from the National Research Council of Canada     

Chromosome stability of cell suspension cultures of Nicotiana spp.

Cell suspension cultures of Nicotiana were initiated using conditions designed to selectively favor stable chromosome number. These conditions included use of leaf explants to initiate cultures, growth of cells in culture medium containing 2,4-D, and transfer of cells with short subculture intervals. Four cell lines derived from Nicotiana tissue with 2n=24, 48, or 72 were established and retain stable chromosome number. Each line could be regenerated to recover plants that retained the somatic chromosome number during culture. Establishment of haploid and diploid cell lines with stable chromosome number is important for mutant isolation and protoplast fusion.     

Ethanol production byZymomonas mobilis in continuous culture at high glucose concentrations

Summary Ethanol production byZ.mobilis has been studied in continuous culture with 10, 15 and 20% glucose media. At 10% glucose, steady state conditions were achieved under glucose-limited conditions. At 15 and 20% glucose, the glucose was not fully metabolized even at low dilution rates and oscillatory behavior was evident. It is proposed that ethanol inhibition of growth is responsible for these phenomena. Comparison of kinetic parameters with those from previously published batch data revealed similar values. The maintenance energy coefficient (m) forZ.mobilis was relatively high and was calculated as 1.6 g/g/h for 10% glucose and 3.1 g/g/h for 15% glucose.