Laboratory scale equipment for the determination of k L a in bio-reactors

The study of the oxygen transfer rate (O.T.R) in reactors designed for cell cultivation and enzyme reaction is a difficult task. In this work a bio-reactor for acetic acid fermentation purposes is studied by using the static gassing out method for K_La evaluation. Results obtained prove that K_La shows linear dependence versus operation temperature.     

Influence of k L a on bioconversion of rice straw hemicellulose hydrolysate to xylitol

The effect of overall oxygen mass transfer coefficient (k_La) on the conversion of xylose to xylitol by Candida guilliermondii FTI 20037 was investigated in batch experiments. Rice straw hemicellulose hydrolysate obtained by acid hydrolysis was employed as a xylose-rich medium. The results showed that this bioconversion strongly depended on the aeration rate. The maximum volumetric productivity (0.52 g/l h^у) and the highest xylitol yield (0.73 g/g) were achieved at an overall oxygen mass transfer coefficient of 15 h^у. Under these conditions 80% efficiency in relation to theoretical yield was attained.     

Effect of antifoam addition on gas-liquid mass transfer in stirred fermenters

The influence of three well-known antifoaming agents (polypropylene glycol, silicone and soybean oil) on gas-liquid mass transfer in stirred tanks is studied, both in model and in fermentation media. The effect of antifoam concentration, ionic strength, viscosity, agitation speed and gas flow rate are investigated. It is found that antifoam addition at low concentrations markedly decreases the gas-liquid volumetric mass transfer coefficient, k_La, for the three antifoam agents tested. Although the major effect is on the film coefficient k_L, some effect is also detected on the specific area, a. It is found that the influence of viscosity and antifoam addition are not cumulative: each tends to attenuate the other's effect on mass transfer. Both for silicone and for soybean oil, but not for PPG in the concentration range studied, there is an antifoam concentration above which further antifoam addition starts to improve k_La.     

Effect of the impeller-sparger configuration over Trichoderma harzianum growth in four-phases cultures under constant dissolved oxygen

Three impeller-sparger configurations were used to evaluate the effect of different hydrodynamic conditions over fungal growth in rheologically complex cultures of Trichoderma harzianum using castor oil as sole carbon source. Three spargers (ring, sintered and 5-orifice) in combination with a turbine impeller system "TIS" (two Rushton turbines) or a hybrid impeller system "HIS" (Rushton turbine and a marine propeller as lower and upper impellers) were used. Their performance was assessed in terms of the response towards disturbance (PID oxygen control settings) and oxygen mass transfer (k_La). To avoid oxygen limitations, all cultures were controlled at 10% DOT by gas blending. Top to bottom mixing, and hence bulk blending, was improved when the - axial flow - HIS was used, ensuring phase interaction and substrate (oil) circulation. The 5-orifice sparger in combination with the TIS configuration yielded the longest lag phase and lowest k_La due to poor bulk blending and to the low gas-liquid interfacial area developed. The highest k_La was achieved with the sintered sparger-HIS probably due to considerable interfacial bubble area enhancement. However, growth limitation occurred as consequence of poor substrate availability as a stable air-oil emulsion was formed at the top of the tank. The best compromise between bulk blending (phase interaction), oxygen transfer (k_La) and fungal growth (growth rate) was achieved with the ring sparger-HIS configuration.     

Vitis vinifera culture in a non-conventional bioreactor: the reciprocating plate bioreactor

This paper is concerned with the potential use of a reciprocating plate bioreactor (RPB) for suspended plant cell cultures. The agitation mechanism of the RPB system, a plate stack, was first evaluated in pure water and in pseudocells medium of 20, 40 and 60% of PCV. As the pseudocell concentration increases, the oxygen mass transfer coefficient, K_La, significantly decreases. Correlations were established for each plate stack and concentration with good prediction of K_La. Three fermentations were performed with Vitis vinifera cells, two in the RPB system and one in shake flasks. Shake flask cultures showed better performance whereas the first fermentation performed with the RPB showed the lowest performance. The lower growth observed was attributed to the operating conditions for aeration and the dissolved oxygen control strategy. CO₂ stripping in the initial portion of the fermentation led to lower biomass growth. The second fermentation, with more appropriate operating conditions, appears to follow the trend of shake flask cultures but was terminated after 5 days due to contamination. The RPB has the potential to be used for suspended plant cell cultures but significant research needs to be performed to find optimal operating conditions but, more importantly, to make appropriate modifications to ensure the sterility of the bioreactor over long time periods.     

General relationship for volumetric oxygen transfer coefficient (k L a) prediction in tower bioreactors utilizing immobilized cells

A general relationship for prediction of the volumetric oxygen transfer coefficient (k_La) in a tower bioreactor utilizing immobilized Penicillium chrysogenum as function of air superficial velocity, suspension rheological parameters and liquid physical properties is proposed in this study. The relationship was applied to three different systems and a good agreement between the calculated values and the experimental data was obtained.     

Determination of power consumption and volumetric oxygen transfer coefficient in bioreactors

A torque meter has been developed for determining the power consumption in a bench stirred tank. The device has been bonded in the stirrer shaft inside a commercial bench fermentor, in order to avoid frictional losses in the mechanical seal. Power consumption measurements in ungassed and gassed systems were obtained at different agitation and aeration conditions, for Newtonian and non-Newtonian fluids. Also, a "simple modified sulfite method" for volumetric oxygen transfer coefficient (k_La) determination was developed and the experimental data were correlated with the gassed power (P_g) by using well-known correlations presented in the literature.     

Oxygen transfer characteristics of a centrifugal, packed-bed reactor during viscous xanthan fermentation

The oxygen transfer properties of a novel, centrifugal, packed-bed reactor (CPBR) during viscous xanthan fermentation were determined with respect to the effects of the arrangement of the centrifugal, packed bed (CPB) and the recirculation loop (RL). Characterized by the maximum volumetric transfer coefficient (k_La) in xanthan broth, the aeration efficiency of CPBR was compared to those in stirred-tank reactors (STR) equipped with disc turbines (DT) or marine propellers (MP), and to that in a water-in-oil emulsion (WIO). As expected, STR-WIO showed the highest k_La (0.038 s^-1 at 2%) among all systems studied due to reduced broth viscosity; however, practical difficulties exist in product recovery. It was found that, at 3.5% xanthan the k_La in CPBR (0.018 s^-1) was higher than that of STR (0.005 s^-1) and close to that of STR-WIO (0.020 s^-1), indicating improved oxygen transfer at such a xanthan concentration. The exterior baffles along the rotating fibrous matrix offer additional agitation in the viscous broth. A gas-continuous arrangement, in which the CPB was kept above the broth, was able to elevate k_La to 0.023 s^-1, higher than that of STR-WIO. The external RL operated by a peristaltic pump was found to play an important role in CPBR aeration by providing better gas-liquid contact. With the improved oxygen transfer efficiency in CPBR at high xanthan concentrations, the CPBR system is practically the preferred system for xanthan fermentation. The characteristic roles of CPB arrangement and the RL should be considered primarily during scale-up operation.     

Characteristics of a DO-controlled fed-batch culture of Escherichia coli

The DO-controlled glucose limited fed-batch technique was investigated in an E. coli process for production of a recombinant protein. The k_Lac^* value (oxygen transfer rate at zero oxygen concentration) was calculated from on-line gas analysis data during the process. In the investigated processes with induced production of recombinant protein, the k_Lac^* value decreased drastically several hours after induction. The reason for the decrease was found in increasing concentrations of DNA in the medium and increased viscosity due to cell lysis. The consequences of such a dramatic decrease in the volumetric oxygen transfer coefficient on the glucose feed and specific rates are described in computer simulations and experimental data.     

Limitation of stomatal conductance by hydraulic traits: sensing or preventing xylem cavitation?

We tested the hypothesis that hydraulic conductance per unit leaf surface area of plant shoots (K_SL) determines the maximum diurnal stomatal conductance (g_L) that can be reached by plants growing in the field. A second hypothesis was tested that some xylem cavitation cannot be avoided by transpiring plants and might act as a signal for regulating g_L. Eleven woody species were studied, differing from each other with respect to taxonomy, wood anatomy and leaf habit. Maximum diurnal g_L, transpiration rate (E_L), pre-dawn and minimum diurnal leaf water potential (O_pd and O_min, respectively) were measured in the field. The critical O level at which stem cavitation was triggered (O_cav) was measured on detached branches, using the acoustic method. A high-pressure flow meter was used to measure maximum K_SL of 1-year-old shoots. Both g_L and E_L were positively related to K_SL. The whole-plant hydraulic conductance per unit leaf area (K_WL) of all the species studied, calculated as the ratio of E_L to (O (=O_pd-O_min) was closely related to K_SL. In every case, O_min (ranging between -0.85 and -1.35 MPa in the different species) dropped to the O_cav range or was <O_cav (ranging between -0.71 and -1.23 MPa), thus suggesting that some cavitation-induced embolism could not be avoided. The possibility is discussed that some cavitation-induced reduction in K_SL is the signal for stomatal closure preventing runaway embolism. The lack of correlation of g_L to O_cav is discussed in terms of the inconsistency of O_cav as an indicator of the vulnerability of plants to cavitation. No differences in hydraulic traits were observed between evergreen and deciduous species.     

Oxygen transfer coefficients by dynamic model moment analysis

A new method to estimate the oxygen transfer coefficient (K_La) from the experimental dynamic response data is presented. Employing a linear model which allows for gas phase, diffusion film, and oxygen electrode dynamics, the first moment of the response curve is simply related to the sum of the model parameters. Two separate experiments are used to characterize the measurement dynamics and to measure the unknown K_La parameter. The simple calculation procedure involves only measuring the area above the response curves.     

Oxygen transfer in Streptomyces fermentation broths

The oxygen transfer coefficient has been investigated in S. noursci and S. lavendulae fermentation broths obtained from fermentors of different operating volumes (61., 30001., 20,0001.). Fermentors had K_La_s values ranging from 1.0 to 17.0 min^?1, calculated from sulphite oxidation rates. The dynamic measurement of the volumetric oxygen transfer coefficient. (K_La) has been performed in the different fermenting systems. As the fermentation progressed, especially in the first stages, K_La values have decreased in both fermentations and in each system of fermentors. In order to characterise the whole fermenting system an average K_La_s was calculated from the obtained K_La values. The average K_La grew with increasing K_La_s values and ranged from 0.03 to 3.72 min^?l. Some factors possibly having an influence on the, change of K_La have been studied. The oxygen transfer coefficients of the broths have been measured in falling films and ranged from 0.05 to 0.4 cm min^?1. The flow conditions have been characterized by Reynolds numbers of broths varying between 1.0 and 60.0. The average thickness of the falling films have been measured and plotted against Reynolds number. The Re⁺ which is the breaking-point of the plot increased as the fermentation proceeded. In the region of Re⁺ the values of the oxygen transfer coefficient increased rapidly. An approximate correlation could be established between the Re⁺ and the physical properties of fermentation broth.     

Study of the oxygen transfer in a disposable flexible bioreactor with surface aeration in vibrated medium

The oxygen mass transfer is a critical design parameter for most bioreactors. It can be described and analyzed by means of the volumetric mass transfer coefficient K _L a. This coefficient is affected by many factors such as geometrical and operational characteristics of the vessels, type, media composition, rheology and microorganism’s morphology and concentration. In this study, we aim to develop and characterize a new culture system based on the surface aeration of a flexible, single-used bioreactor fixed on a vibrating table. In this context, the K _L a was evaluated using a large domain of operating variables such as vibration frequency of the table, overpressure inside the pouch and viscosity of the liquid. A novel method for K _L a determination based on the equilibrium state between oxygen uptake rate and oxygen transfer rate of the system at given conditions was also developed using resting cells of baker’s fresh yeast with a measured oxygen uptake rate of 21 mg g⁻¹ h⁻¹ (at 30°C). The effect of the vibration frequency on the oxygen transfer performance was studied for frequencies ranging from 15 to 30 Hz, and a maximal K _L a of 80 h⁻¹ was recorded at 30 Hz. A rheological study of the medium added with carboxymethylcellulose at different concentrations and the effect of the liquid viscosity on K _L a were determined. Finally, the mixing time of the system was also measured using the pH method.     

Influence of climate-driven shifts in biomass allocation on water transport and storage in ponderosa pine

Conifers decrease the amount of biomass apportioned to leaves relative to sapwood in response to increasing atmospheric evaporative demand. We determined how these climate-driven shifts in allocation affect the aboveground water relations of ponderosa pine growing in contrasting arid (desert) and humid (montane) climates. To support higher transpiration rates, a low leaf:sapwood area ratio (A_L/A_S) in desert versus montane trees could increase leaf-specific hydraulic conductance (K_L). Alternatively, a high sapwood volume:leaf area ratio in the desert environment may increase the contribution of stored water to transpiration. Transpiration and hydraulic conductance were determined by measuring sap flow (J_S) and shoot water potential during the summer (June-July) and fall (August-September). The daily contribution of stored water to transpiration was determined using the lag between the beginning of transpiration from the crown at sunrise and J_S. In the summer, mean maximum J_S was 31.80LJ.74 and 24.34Dž.05 g m^-2 s^-1 for desert and montane trees (a 30.6% difference), respectively. In the fall, J_S was 25.33NJ.52 and 16.36dž.64 g m^-2 s^-1 in desert and montane trees (a 54.8% difference), respectively. J_S was significantly higher in desert relative to montane trees during summer and fall (P<0.05). Predawn and midday shoot water potential and sapwood relative water content did not differ between environments. Desert trees had a 129% higher K_L than montane trees in the summer (2.41᎒^-5 versus 1.05᎒^-5 kg m^-2 s^-1 MPa^-1, P<0.001) and a 162% higher K_L in the fall (1.97᎒^-5 versus 0.75᎒^-5 kg m^-2 s^-1 MPa^-1, P<0.001). Canopy conductance decreased with D in all trees at all measurement periods (P<0.05). Maximum g_C was 3.91 times higher in desert relative to montane trees averaged over the summer and fall. Water storage capacity accounted for 11 kg (11%) and 10.6 kg (17%) of daily transpiration in the summer and fall, respectively, and did not differ between desert and montane trees. By preventing xylem tensions from reaching levels that cause xylem cavitation, high K_L in desert ponderosa pine may facilitate its avoidance. Thus, the primary benefit of low leaf:sapwood allocation in progressively arid environments is to increase K_L and not to increase the contribution of stored water to transpiration.     

Zur Maßstabsübertragung von aeroben mikrobiologischen Prozessen Teil I. Stofftransport

Because the interior scale of turbulence in reinforced bioreactors is essentially greater than the particles of bacteria or yeasts, the mass transfer occurs at the particles only in consequence of the molecular diffusion and depends on the concentration of the soluted material only. As a decided criterion for the transmission of scale in such processes is considered the volumetric oxygen transfer coefficient K_La This article practises a theoretical analysis of the characteristic hydrodynamic conditions in bubble columns and in agitators: the content of gas, the specific area of mass transfer and the coefficient of mass transfer K_L. These conditions are joined with the evaluation of the K_La value. Resultant the data of calculation hence it follows a computational determination of the K_La value by means of the physical matter values, the construction of devises and the process conditions.     

A novel split-cylinder airlift reactor for fed-batch cultures

Conventional airlift reactors are not adequate to carry out variable volume processes since it is not possible to achieve a proper liquid circulation in these reactors until the liquid height is higher than that of the downcomer. To carry out processes of variable volume, the use of a split-cylinder airlift reactor is proposed, in the interior of which two multi-perforated vertical baffles are installed in order to provide several points of communication between the reactor riser and downcomer. This improves the liquid circulation and mixing at any liquid volume. In fed-batch cultures, it is important to know how liquid height affects the hydrodynamic characteristics and the volumetric oxygen transfer coefficient since this impacts on the kinetic behavior of any fermentation. Thus, in the present work, the effect of the liquid height on the mixing time, the overall gas hold-up, and the volumetric oxygen transfer coefficient of the proposed airlift reactor were determined. The mixing time was increased and the volumetric oxygen transfer coefficient decreased due to the increase of the liquid height in the reactor in all the superficial gas velocities tested, which corresponded to a pseudohomogeneous flow regime. The experimental values of the mixing time and the mass-transfer coefficient were properly described through correlations in which the U_GR/H_L ratio was used as the independent variable. Thus, this variable might be used to describe the hydrodynamic behavior and the oxygen transfer coefficient of airlift reactors when such reactors are used in processes where the liquid volume changes with time. However, these correlations are useful for the particular device and for the particular operating conditions at which they were obtained. These empirical correlations are useful to understand some factors that influence the mixing time and volumetric oxygen transfer coefficient, but such correlations do not have a sufficient predictive potential for a satisfactory reactor design. The overall gas hold-up values were not significantly affected when the liquid height was lower than the downcomer height. However, the values decreased abruptly when the reactor was operated with liquid heights over the downcomer height, especially at high superficial gas velocities.     

CO2 exchange and thallus nitrogen across 75 contrasting lichen associations from different climate zones

Aiming to investigate whether a carbon-to-nitrogen equilibrium model describes resource allocation in lichens, net photosynthesis (NP), respiration (R), concentrations of nitrogen (N), chlorophyll (Chl), chitin and ergosterol were investigated in 75 different lichen associations collected in Antarctica, Arctic Canada, boreal Sweden, and temperate/subtropical forests of Tenerife, South Africa and Japan. The lichens had various morphologies and represented seven photobiont and 41 mycobiont genera. Chl a, chitin and ergosterol were used as indirect markers of photobiont activity, fungal biomass and fungal respiration, respectively. The lichens were divided into three groups according to photobiont: (1) species with green algae, (2) species with cyanobacteria, and (3) tripartite species with green algal photobionts and cyanobacteria in cephalodia. Across species, thallus N concentration ranged from 1 to 50 mg g^-1 dry wt., NP varied 50-fold, and R 10-fold. In average, green algal lichens had the lowest, cyanobacterial Nostoc lichens the highest and tripartite lichens intermediate N concentrations. All three markers increased with thallus N concentration, and lichens with the highest Chl a and N concentrations had the highest rates of both P and R. Chl a alone accounted for ca. 30% of variation in NP and R across species. On average, the photosynthetic efficiency quotient [K_F=(NP_max+R)/R)] ranged from 2.4 to 8.6, being higher in fruticose green algal lichens than in foliose Nostoc lichens. The former group invested more N in Chl a and this trait increased NP_max while decreasing R. In general terms, the investigated lichens invested N resources such that their maximal C input capacity matched their respiratory C demand around a similar (positive) equilibrium across species. However, it is not clear how this apparent optimisation of resource use is regulated in these symbiotic organisms.     

Improved method for the dynamic measurement of mass transfer coefficient for application to solid–substrate fermentation

A new method has been developed for the measurement of overall volumetric mass transfer coefficient (K_L a) in gas-liquid-solid systems. This method is based on the examination of gas phase dynamics in a three-phase contactor and consists of measuring continuously the response of the outlet gas composition to a step input change of CO₂ in the inlet gas stream. The advantages and limitations of the new method are presented and its sensitivity is discussed on the basis of model predictions. Preliminary results on the implementation of the CO₂ method are also reported. Experimental data obtained in a nonviscous electrolyte solution show that the proposed method compares favorably with the conventional dissolved oxygen technique, provided that a correction is made to take account of the difference in diffusivity of oxygen and carbon dioxide.     

A kLa identification technique for a dynamic model of the coupled system: Air-lift fermenter — oxygen probes

The time delay of oxygen probe response to the signal from a fermenter makes identification of the volumetric oxygen transfer coefficient k_La by the dynamic method more complicated. A coupled model involving the transient-state oxygen balance of the fermenter together with the dynamic model of the oxygen probe must be then formulated, solved and identified. In this paper two simple models of air-lift loop fermenters have been proposed and a coupled mathematical model of the fermenter – oxygen probe system has been developed. The identification procedure was used to estimate k_La values in the fermenter with internal circulation flow on the basis of experimental measurements. A comparison of evaluated and experimental indications of the probes placed at various heights of the column proves that the model presented gives a possibility of the first-step approximation of k_La in loop fermenters.     

Determination of volumetric oxygen transfer coefficient by off-gas analysis

In various aerobic bioreactors including activated sludge aeration tanks, the volumetric mass transfer coefficient K_La is frequently used as an estimate of the rate of oxygen dissolution into the liquid phase. The K_La measurement in such bioreactors is widely applied with the aid of sodium sulfite (Na₂SO₃) as an oxygen-consuming substance used to maintain low dissolved oxygen concentration. In the present study, the effect of the addition of Na₂SO₃ on K_La, determined by an off-gas analysis, was investigated specifically from the viewpoint of variations in the size of air bubbles and the enhancement factor associated with the change in sulfite concentration. Experiments were conducted in a draft-tube bubble column, using a zirconia electrode oxygen analyzer for measurement of the O₂ mole fraction in the exhaust gas and a dual electrical resistivity probe for measurement of the bubble size. It was found that the increase in the specific gas-liquid interfacial area, resulting from bubble size reduction effected by Na₂SO₃ functioning as an electrolyte, is more pronounced than the enhancement of the absorption rate through the interface. The upper limit of Na₂SO₃ concentration for sustaining physical absorption, in the absence of any catalyst, ranges from 30 to 70 mol/m³, while that for preventing the average bubble size from decreasing is about 15 mol/m³. Furthermore, to secure a reliable K_La measurement, the K_La value should not exceed 50 h⁻¹ for the liquid depth of 3 m even when the limiting conditions are not exceeded. The off-gas analysis proposed in this study for K_La determination is expected to be extremely useful provided that the above conditions are fulfilled, since it only requires moderate addition of the sulfite as the oxygen-consuming substance and will not interrupt the reactor operation as long as oxygen uptake occurs in the system.