A re-examination of the problem of photochemical nitrogen reduction by blue-green algae

Summary Although it was possible in the light in the absence of carbon dioxide to obtain a ratio of nitrogen fixed to oxygen evolved in nitrogen-starved cells of A. cylindrica near to 1:1.5, that quoted by other workers, ratios varying between 1:0.9 and 1:3.0 were also obtained. The amount of oxygen evolved under the same conditions by normal cells in the presence of pyruvate was increased considerably. Since the addition of pyruvate also resulted in increased carbon dioxide output in the dark with the same algal material, oxygen output in the light was attributed to the production of factors necessary for carbon assimilation.Addition of pyruvate to nitrogen-starved and normal cells in the light resulted in similar rates of oxygen evolution after an initially higher rate in the starved cells. The ratio of overall nitrogen fixed to oxygen evolved, was 1:6.6 for the starved cells and 1:6.4 for the normal cells, showing that the presence of an added substrate increased oxygen output relative to nitrogen uptake. ¹⁴CO₂ was recovered from sodium pyruvate-1-¹⁴C in flasks incubated in the dark, showing that, at least in the dark, pyruvate was decarboxylated.The interpretation of these results is that endogenous and exogenous substrates available to cells of A. cylindrica become decarboxylated and that, in the light, carbon dioxide produced may be assimilated photochemically with accompanying oxygen evolution. This interpretation has been discussed in relation to reports of photochemical nitrogen reduction in blue-green algae.     

Measurement of oxygen uptake and carbon dioxide production rates ofmammalian cells using membrane mass spectrometry

A method for the measurement of oxygen uptake and carbon dioxide production rates in mammalian cell cultures using membrane mass spectrometry is described. The small stirred reactor with a volume of 15 ml and integrated pH-control permits the economical application of isotopically labelled substrates and ¹³C-labelled bicarbonate buffer. Repetitive experiments showed the reproducibility of the method. In one case bicarbonate-free HEPES buffer was used and carbon dioxide production was measured using the intensity of the peak at m/z = 44(¹²CO₂). In all other cases H¹³CO₃ ⁻ -buffer was applied and also¹²CO₂ was measured. The minimum cell density required was only 2 × 10⁴ cells ml⁻¹. In the hybridoma T-flask cultivation studied here the measured specific oxygen uptake and carbon dioxide production rates were reasonably constant during the exponential growth phase and decreased significantly afterwards. Estimated respiratory quotients were always between0.90 and 0.92 except in HEPES-buffer, where a value of 0.67 was found. In the latter case specific oxygen uptake rate was higher than in bicarbonate buffered culture, however, carbon dioxide production rate was lower, and viable cell density was lowest. The addition of phenazine methosulfate, an artificial electron acceptor, increased both rates resulting in highest viable cell density but also highest lactate production rate. Glucose and glutamine pulse-feeding increased final cell density. The method described is directly applicable for samples from batch, fed-batch and continuous cultivations. This revised version was published online in August 2006 with corrections to the Cover Date.     

A sensitive monitoring system for mammalian cell cultivation processes: a PAT approach

Biopharmaceuticals such as antibodies are produced in cultivated mammalian cells, which must be monitored to comply with good manufacturing practice. We, therefore, developed a fully automated system comprising a specific exhaust gas analyzer, inline analytics and a corresponding algorithm to precisely determine the oxygen uptake rate, carbon dioxide evolution rate, carbon dioxide transfer rate, transfer quotient and respiratory quotient without interrupting the ongoing cultivation, in order to assess its reproducibility. The system was verified using chemical simulation experiments and was able to measure the respiratory activity of hybridoma cells and DG44 cells (derived from Chinese hamster ovary cells) with satisfactory results at a minimum viable cell density of ~2.0 × 10⁵ cells ml^?1. The system was suitable for both batch and fed-batch cultivations in bubble-aerated and membrane-aerated reactors, with and without the control of pH and dissolved oxygen.     

Detection of ginkgolide A in Ginkgo biloba cell cultures

Ginkgo biloba cells were cultured in two 500 mL shake flasks and in 2 L and 6 L immobilization bioreactors using MS medium supplemented with 1 mg.L^–1 NAA, 0.1 mg.L^–1 K and 30 g.L^–1 sucrose. Specific growth rates were 0.06 d^–1, 0.11 d^–1 and 0.07 d^–1 for the 2 L and 6 L bioreactors and shake flask cultures, respectively. Extracellular phosphate, nitrate, ammonium and carbohydrate uptake rates of the bio reactor cultures were approximately 17 to 39% slower than those of shake flask cultures. The specific oxygen uptake and carbon dioxide transfer rates of immobilized Ginkgo biloba cells ranged from 0.027 to 0.041 mmol O₂.g^–1.d.w.hr^–1 (maximum uptake at 14 days) and 0.020 to 0.057 mmol CO₂g. ^–1.d.w.hr^–1 (maximum production at 14 days). Extracts from the biomass of the two immobilized and shake flask suspension cultures were analysed for ginkgolide A by GC-MS. Yields of 7, 17, 19 and 7 ng.g. ^–1d.w. of ginkgolide A were determined for shake flask 1, shake flask 2 and the 2 L and 6 L immobilized cultures, respectively. Traces of ginkgolide B were detected with the signal to noise ratio, however, being too low for positive confirmation of this last product.Abbreviations CTR Carbon dioxide transfer rate - DO Dissolved oxygen - g.d.w. Gram dry weight - GA Ginkgolide A - GB Ginkgolide B - GC Gas chromatography - GC-MS Gas chromatography-mass spectrometry - HPLC High performance liquid chromatography - K Kinetin - MS Murashige and Skoog salt medium - N₁K₁MS Complete Murashige and Skoog medium supplemented with 1 mg.L^–1 NAA, 0.1 mg.L^–1 K and 30g.L^–1 sucrose - NAA Naphthaleneacetic acid - OTR Oxygen transfer rate - PAF Platelet Aggregating Factor - q_CO2 Specific carbon dioxide production rate - q_O2 Specific oxygen uptake rate - u Specific growth rate     

GLYCOLYSIS IN RAT PERITONEAL MAST CELLS

Glycolytic activity of rat peritoneal mast cells has been measured by the Cartesian ampulla diver technique. The rates of anaerobic glycolysis, expressed as CO₂ expelled from a bicarbonate medium, are 1.70 x 10^-6 µl and 1.43 x 10^-6 µl per cell per hour with and without glucose, respectively. The aerobic glycolysis rate in the presence of glucose, assuming the respiratory quotient to be 1, is 0.93 x 10^-6 µl CO₂ per cell per hour. It is pointed out that the anaerobic and non-respiratory aerobic carbon dioxide production by mast cells is much higher than the respiratory oxygen uptake reported previously. These values have been interpreted in terms of glucose utilization.     

CO2 in large-scale and high-density CHO cell perfusion culture

Productivity in a CHO perfusion culture reactor was maximized when pCO₂ was maintained in the range of 30–76 mm Hg. Higher levels of pCO₂ (> 150 mm Hg) resulted in CHO cell growth inhibition and dramatic reduction in productivity. We measured the oxygen utilization and CO₂ production rates for CHO cells in perfusion culture at 5.55×10^-17 mol cell^-1 sec^-1 and 5.36×10^-17 mol cell^-1 sec^-1 respectively. A simple method to directly measure the mass transfer coefficients for oxygen and carbon dioxide was also developed. For a 500 L bioreactor using pure oxygen sparge at 0.002 VVM from a microporous frit sparger, the overall apparent transfer rates (k_La+k_AA) for oxygen and carbon dioxide were 0.07264 min^-1 and 0.002962 min^-1 respectively. Thus, while a very low flow rate of pure oxygen microbubbles would be adequate to meet oxygen supply requirements for up to 2.1×10⁷ cells/mL, the low CO₂ removal efficiency would limit culture density to only 2.4×10⁶ cells/mL. An additional model was developed to predict the effect of bubble size on oxygen and CO₂ transfer rates. If pure oxygen is used in both the headspace and sparge, then the sparging rate can be minimized by the use of bubbles in the size range of 2–3 mm. For bubbles in this size range, the ratio of oxygen supply to carbon dioxide removal rates is matched to the ratio of metabolic oxygen utilization and carbon dioxide generation rates. Using this strategy in the 500 L reactor, we predict that dissolved oxygen and CO₂ levels can be maintained in the range to support maximum productivity (40% DO, 76 mm Hg pCO₂) for a culture at 10⁷ cells/mL, and with a minimum sparge rate of 0.006 vessel volumes per minute.A = volumetric agitated gas-liquid interfacial area at the top of the liquid, 1/mB = cell broth bleeding rate from the vessel, L/minCER = carbon dioxide evolution rate in the bioreactor, mol/min[CO₂] = dissolved CO₂ concentration in liquid, M[CO₂]^* = CO₂ concentration in equilibrium with sparger gas, M[CO₂]^** = CO₂ concentration in equilibrium with headspace gas, MCO₂(1) = dissolved carbon dioxide molecule in water[C_T] = total carbonic species concentration in bioreactor medium, M[C_T]_F = total carbonic species concentration in feed medium, MD = bioreactor diameter, mD_I = impeller diameter, mD_b = the initial delivered bubble diameter, mF = fresh medium feeding rate, L/minH_L = liquid height in the vessel, mk_A = carbon dioxide transfer coefficient at liquid surface, m/mink _infA ^supO = oxygen transfer coefficient at liquid surface, m/minNomenclature     

Photoproduction of Hydrogen by the Marine Heterocystous Cyanobacterium Anabaena Species TU37-1 Under a Nitrogen Atmosphere

Hydrogen production rates by Anabaena sp. strain TU37-1 obtained after an initial 1-day incubation period were approximately 70 to 80 and 3 to 9 µmol (mg chl)^–1 h^–1 under argon and nitrogen atmospheres, respectively. Hydrogen production under argon was not enhanced by addition of carbon dioxide, but was enhanced to some extent under nitrogen by increasing the initial carbon dioxide concentration. Rates of hydrogen and oxygen production during the initial 7-hour period were 15 and 220 µmol (mg chl)^–1 h^–1, respectively, in vessels with 18.5% initial carbon dioxide. Hydrogen production under nitrogen was enhanced by addition of carbon monoxide (1%). The rate obtained from the initial 1-day incubation period was about 40 µmol (mg chl)^–1 h^–1, which corresponded to about 60% of that under argon. On the basis of these observations, a possible strategy for hydrogen production by nitrogen-fixing cyanobacteria under nitrogen in the presence of carbon monoxide is indicated.     

Bubble free gaseous transfer in bioreactors using perfluorocarbons

In this work the concept of bubble-free oxygenation that was able to ensure oxygen supply and carbon dioxide extraction for a chemostat culture of Escherichia coli was experimentally demonstrated. It was operated at the dilution rate of 0.275 h^–1 under atmospheric pressure and at 35.5 °C. Foralkyl, a commercial perfluorocarbon, added in the influent medium under emulsified form and at 50% volumic fraction, was able to provide 0.17 g O₂/l/h and extract 0.23 g CO₂/l/h for a culture at 0.74 g/l of biomass. This oxygen supply was close to the maximum oxygenation Foralkyl was theoretically able to provide at this pressure when imposing a minimum oxygen concentration of 1 mg/l in the water phase. The quantification of transfer was not done from a direct measurement of oxygen transfer rates because conventional oxygen concentration measurement by membrane polarographic probe in an emulsion was not judged reliable. This evaluation was done by referring to conventional aerated culture whose measurable parameters (biomass and product concentrations) were found unaffected when shifting to the novel oxygenation device.List of Symbols C _LV ^* , C _LV g/l dissolved oxygen concentration in the vector phase at equilibrium and in the reactor - C _LW ^* , C _LW g/l dissolved oxygen concentration in the water phase at equilibrium and in the reactor - C _LWinput , C _LWoutput g/l dissolved oxygen concentrations in aqueous medium in the reactor input and output flow - D h^–1 dilution rate - ^DMM_{o 2}, MM_{co 2} g/mol oxygen and carbon dioxide molar masses - %O_2input, %O_2output oxygen percentages in the reactor input and output flow - %CO_2input, %CO_2output carbon dioxide percentages in the reactor input and output flow - %N _2input %N _2output nitrogen percentages in the reactor input and output flow - Q _G.i ⁿ Q _G.o ⁿ l/h gas flow rates at the reactor input and output at normal conditions (273 K, 1 atm) - Q _L l/h liquid flow rate - Q _LW , Q _LV l/h water and vector flow rates - r_{O 2} g/l/h oxygen consumption rate - r _x g/l/h biomass production rate - r _{CO 2} g/l/h carbon dioxide production rate - V _L l fermentor aqueous volume - V _LW , V _LV l water phase and vector phase volume - V _{O 2}, V _{CO 2}, l/mol oxygen and carbon dioxide molar volume under gaseous form at normal conditions (273 K, 1 atm) - Y _{O 2 x} gO₂/g cell oxygen consumption yield for biomass growth - Y _sx g glucose/g cell glucose consumption yield for biomass growth - vector volumic fraction - h^–1 growth rate This work was totally financed by the European Space Agency.     

Data consistency,yield, maintenance,and hysteresis in batch cultures of Candida lipolytica cultured on n-hexadecane

Candida lipolytica was cultured batchwise using n-hexadecane as the main carbon source. Biomass production, n-hexadecane consumption, oxygen consumption, and carbon dioxide evolution were measured to follow the fermentation. The consistency of the measured data was examined using integrated and instantaneous available electron and carbon balances. Values of the “true” growth yield, η_max, and maintenance coefficient, m_e were estimated using three different sets of data (biomass and n-hexadecane, oxygen and biomass, and CO₂ and biomass), and the results were compared with estimates obtained from literature data. Hysteresis patterns were observed in plots of specific rates of oxygen consumption and carbon dioxide evolution versus specific growth rate.     

Gas phase composition effects on suspension cultures of Taxus cuspidata

The effect of different concentrations and combinations of oxygen, carbon dioxide, and ethylene on cell growth and taxol production in suspension cultures of Taxus cuspidata was investigated using several factorial design experiments. Low head space oxygen concentration (10% v/v) promoted early production oftaxol. High carbon dioxide concentration (10% v/v) inhibited taxol production. The most effective gas mixture composition in terms of taxol production was 10% (v/v) oxygen, 0.5% (v/v) carbon dioxide, and 5 ppm ethylene. Cultures grown underambient concentration of oxygen had a delayed uptake of glucose and fructose compared to cultures grown under 10% (v/v) oxygen. Average calcium uptake rates into the cultured cells decreased and average phosphate uptake rates increased as ethylene was increased from 0 to 10 ppm. These results may indicate that gas composition alters partitioning of nutrients, which in turn affects secondary metabolite production. (c) 1995 John Wiley & Sons, Inc.     

STUDIES OF CARBON AND NITROGEN METABOLISM BY THREE MARINE PHYTOPLANKTON SPECIES IN NITRATE-LIMITED CONTINUOUS CULTURE1,2

Characteristics of carbon production, excretion and dark respiration, and nitrate uptake kinetics were studied using continuous culture techniques for Thalassiosira allenii Takano, Monorhrysis lutheri Droop and Dunaliella tertiolccta Butcher. Fur T. allenii. the ratio of dark C loss to daytime net C production varied between 0.1 and 0.2 over a growth rate range from ca. 0.005 to 0.06 h^-1. For M. lutheri and D. tertiolecta. this same ratio varied belween 0.2 and 0.3 between growth rates of ca. 0.005 and 0.025 h^-1, but declined at higher growth rates when the dark nitrate uptake capacity of the cells was exceeded by the pumping rate. Carbon excretion rates averaged less than 1.5% of daytime net C production rates. Productivity indices showed little correlation with growth rate, due to the significant poisitive correlation between chl a:C ratios and growth rate. Chlorophyll a:C ratios for T. allenii were less than 0.01 al growth rates less than 0.03 h^-1, and appoached zero at zero growth rate. Dark nitrate maximum uptake rates for M. lutheri, D. tertiolecta and T. allenii averaged 23, 64 and 120%, respectively, of light nitrate maximum uptake rates. Excretion of nitrite was observed during most nitrate uptake experiments. This excretion reduced net uptake of nitrate spikes in the dark for M. lutheri and D. tertiolecta by 79 and 23%, respectively.     

Ion exchange resin: A model support for solid state growth fermentation of Aspergillus niger

An ion exchange resin (Amberlite IRA -900) impregnated with a defined media was used as support for the growth of Aspergillus niger. Growth started 8 hours after spore inoculation and attained a maximum biomass concentration at 24 hours. The maximum oxygen uptake and carbon dioxide production rates were achieved at 17 hours. Growth had a strong correlation with the pressure drop in the fermenters.     

An analysis of the growth of Gluconobacter oxydans in chemostat cultures

Gluconobacter oxydans was grown successively in glucose and nitrogen-limited chemostat cultures. Construction of mass balances of organisms growing at increasing dilution rates in glucose-limited cultures, at pH 5.5, revealed a major shift from extensive glucose metabolism via the pentose phosphate pathway to the direct pathway of glucose oxidation yielding gluconic acid. Thus, whereas carbon dioxide production from glucose accounted for 49.4% of the carbon input at a dilution rate (D)=0.05 h^-1, it accounted for only 1.3% at D=0.26 h^-1. This decline in pentose phosphate pathway activity resulted in decreasing molar growth yields on glucose. At dilution rates of 0.05 h^-1 and 0.26 h^-1 molar growth yields of 19.5 g/mol and 3.2 g/mol, respectively, were obtained. Increase of the steady state glucose concentration in nitrogen-limited chemostat cultures maintained at a constant dilution rate also resulted in a decreased flow of carbon through the pentose phosphate pathway. Above a threshold value of 15–20 mM glucose in the culture, pentose phosphate pathway activity almost completely inhibited. In G. oxydans the coupling between energy generation and growth was very inefficient; yield values obtained at various dilution rates varied between 0.8–3.4 g/cells synthesized per 0.5 mol of oxygen consumed.     

Effects of Humidity on Photosynthesis

It was found for two species that net carbon dioxide uptakerates were reduced at constant intercellular carbon dioxidepartial pressure when single attached leaves were exposed tolarge leaf to air water vapour pressure differences. Leaf temperature,irradiance, and ambient carbon dioxide and oxygen partial pressureswere kept constant. Net carbon dioxide uptake rates decreasedlinearly with increasing vapour pressure difference, even incases where transpiration rates were highest at intermediatevalues of vapour pressure difference. Decreases in net carbondioxide uptake rates were quickly reversible. Different windspeeds across the measured leaf, different vapour pressure deficitsaround the rest of the shoot, and transient responses of netcarbon dioxide uptake rate to abrupt changes in vapour pressuredifference all gave the same response of net carbon dioxideuptake rate to vapour pressure difference. The data show thatthe inhibition of net carbon dioxide uptake rate at a givenvapour pressure difference was not simply related to whole leaftranspiration rate or stomatal conductance. Key words: Vapour pressure difference, CO₂ uptake rate, Leaf temperature     

Participations of Iron and Flavin Adenine Dinucleotide on the Enzymatic Hydroxylation of p-Hydroxybenzoate.

The effects of oxygen and carbon dioxide in inosine fermentation were investigated from the industrial viewpoint. Oxygen supply at the rate of more than 5 × 10^-7 mole/ml-min was indispensable for maintaining the high productivity of inosine in jar fermentors as well as in shaking flasks. Oxygen deficiency due to insufficient oxygen supply, on the other hand, resulted in the inhibition of inosine production, even though glucose added to the medium was entirely assimilated. In addition to sufficient oxygen supply ventilation was also indispensable since an increased tension of carbon dioxide reduced the inosine-producing capability of the cells.     

The consequence of stimulating glucose dehydrogenase activity by the addition of PQQ on metabolite production by Agrobacterium radiobacter NCIB 11883

Summary Agrobacterium radiobacter NCIB 11 883 does not produce gluconate under conditions of glucose excess in batch or continuous culture. However, the addition of micromolar concentrations of pyrrolo quinoline quinone (PQQ) to fermentation media resulted in rapid excretion of gluconate by batch and continuous cultures. This rapid dehydrogenation of glucose was found in cells grown under carbon and nitrogen limitation and is constitutive which suggests that the only reason why this activity is not normally expressed is due to the inability of the organism to synthesize the prosthetic group (PQQ) of the glucose dehydrogenase enzyme.Although the addition of PQQ to batch and continuous cultures caused a very rapid specific rate of gluconate production (0.6–1.1 g gluconate g^-1 dry wt. h^-1) the rate of exopolysaccharide production remained unaltered. Indeed, when the rates of substrate and oxygen uptake are corrected for the rate of gluconate production in the presence of PQQ there appears to be little physiological consequence as a result of this oxidation.     

Effect of oxygen and carbon dioxide on germination and growth ofRhizopus oligosporus on model media and soya beans

 The microcolony technique enables the effects of several atmospheric conditions on fungal growth to be studied by measuring the radius of the colony, while excluding effects of those conditions on germination of the sporangiospores. Various concentrations of oxygen and carbon dioxide in the gas environment were found to influence growth of Rhizopus oligosporus on malt extract/soya peptone/agar. The maximum radial growth rate was 1.48 mm/h and the maximum specific growth rate was 0.109 h^-1 at 30 °C. Oxygen became limiting below 1% (v/v), but growth remained possible at levels of 0.001% oxygen. Carbon dioxide stimulated growth at limiting oxygen levels. The specific growth rate increased from 0.043 h^-1 at 0.5% (v/v) oxygen and 0% (v/v) carbon dioxide to 0.096 h^-1 at 0.5% (v/v) oxygen and 5% (v/v) carbon dioxide. A mixture of 0.5% (v/v) oxygen and 35% (v/v) carbon dioxide inhibited growth. Delay of sporangiospore germination due to low (less than 0.001%) amounts of oxygen was not observed with the techniques used. Fungal activity in a rotating drum fermentor was more strongly affected by low levels of oxygen than was biomass formation on model media. High concentrations of carbon dioxide inhibited growth in the rotating drum fermentor at non-limiting levels of oxygen. It is concluded that aeration and heat removal are both essential aspects of optimization of large-scale solid-substrate bioreactors with Rh. oligosporus. Received: 5 August 1994/Received revision: 14 November 1994/Accepted: 5 December 1994     

Xylitol formation by Candida boidinii in oxygen limited chemostat culture

Summary Production of xylitol by Candida boidinii NRRL Y-17213 occurs under conditions of an oxygen limitation. The extent to which substrate is converted to xylitol and its coproducts (ethanol, other polyols, acetic acid), and the relative flow rates of substrate to energetic and biosynthetic pathways is controlled by the degree of oxygen limitation.With decrease in oxygen concentration in the inlet gas, for a constant dilution rate of 0.05 1/h. the specific oxygen uptake rate decreased from 1.30 to 0.36 mmol/gh Xylitol was not produced at specific oxygen uptake rates above 0.91 mmol/gh. Upon shift to lower oxygen rates, specific xylitol production rate increased more rapidly than specific ethanol production rate:Nomenclature D dilution rate (1/h) - DOT dissolved oxygen tension (%) - m_o2 maintenance coefficient (mmol O₂/g cell mass h) - q_o2 specific oxygen uptake rate (mmol O₂/g cell mass h) - q_s specific xylose uptake rate (g xylose/g cell mass h) or (mmol xylose/g cell mass h) - q_x specific xylitol production rate (g xylitol/ g cell mass h) or (mmol xylitol/ g cell mass h) - q_e specific ethanol production rate (g ethanol/ g cell mass h) or (mmol ethanol/ g cell mass h) - q_CO2 specific carbon dioxide production rate (mmol CO₂/g cell mass h) - S xylose concentration (g/1) - Y_cm/s cell mass yield coefficient, (g cell mass/mmol xylose) or (g cell mass/ g xylose consumed) - Y_cm/O2 cell mass yield coefficient, (g cell mass/mmol O₂) - Y_X/S xylitol yield coefficient (g xylitol/g xylose consumed) - Y_x/O2 xylitol yield coefficient (g xylitol/mmol O₂) - Y_e/s ethanol yield coefficient (g ethanol/g xylose consumed) - OUR oxygen uptake rate (mmol O₂/1h) - specific growth rate (1/h)     

Growth of a Catharanthus roseus cell suspension culture in a modified chemostat under glucose-limiting conditions

Summary A system for the continuous cultivation of plant cells has been developed, based on a commercially available 3–1 turbine-stirred fermentor. A special device was constructed to provide for homogeneous effluent from the culture at low dilution rates. Two steady states with Catharanthus roseus cells growing under glucose limitation are described with respect to biomass yield on the carbon and energy source glucose, specific oxygen consumption, specific carbon dioxide production and (by)product formation. From a carbon balance for each steady state it is shown that the flow of carbon to the culture (as glucose) practically equalled the flow of carbon from the culture (as biomass, carbon dioxide and (by)product). Biomass yields on glucose were 0.31 g/g and 0.35 g/g at dilution rates of 0.0060 l/h and 0.0081 l/h respectively. The striking difference between the obtained yield coefficients and biomass yield commonly found for batch-cultured plant cells is discussed.     

Glutamic acid production in an airlift reactor with net draft tube

Cultivation of Brevibacterium divaricatum for glutamic acid production in an airlift reactor with net draft tube was developed. Cell concentration gave an index for adding penicillin G. On-line estimation of total sugar concentration yielded an identified model which was used for determination of the substrate addition. Fermentation for glutamic acid production requires high oxygen concentration in the broth. The proposed reactor has the capability to provide sufficient oxygen for the fermentation. Since the reactor is suitable for fed-batch culture, the cultivation of B. divaricatum for glutamic acid production in the proposed reactor is successfully carried out.List of Symbols a system parameter - b system parameter - C _c,in mole fraction carbon dioxide in the gas inlet - C _c,out mole fraction carbon dioxide in the gas outlet - C _L mole/dm³ oxygen concentration in liquid phase - C _L ^* mole/dm³ saturated oxygen concentration in liquid phase - C _0,in mole fraction of oxygen in the gas inlet - C _0,out mole fraction of oxygen in the gas outlet - CPR mole/h/dm³ carbon dioxide production rate based on total broth - E(t) error signal - F _in mole/h inlet gas flow rate - k ₁ constant defined by Eq. (4) - k ₂ constant defined by Eq. (5) - k _L a 1/h volumetric mass transfer coefficient of gas-liquid phase - OUR mole/h/dm³ oxygen uptake rate based on total broth - P atm pressure in the reactor - t h time - TS _c g total sugar consumption - TS _s g/dm³ set point of total sugar concentration - TS _* g/dm³ reference value of total sugar concentration - TS(t) g/dm³ total sugar concentration in the broth at timet - u(t) cm³/min feed rate at timet - V dm³ total broth volume - VVM (dm³/min)/dm³ flow rate per unit liquid volume - a negative constant defined by Eq. (7)