Effect of specific growth rates on productivity in continuous open and partial cell retention animal cell bioreactors.

A clonal derivative of a transfectant of the SP2/0 myeloma cell line producing a chimeric monoclonal antibody was cultivated in both continuous open and continuous partially-closed bioreactors. Using an open system for the determination of kinetic parameters, we showed that the production of this chimeric mAb was growth associated. As such, the volumetric productivity increased linearly with increasing dilution rate up to the maximum dilution rate. Three continuous cultivations employing partial cell retention were conducted. In agreement with mathematical predictions, the product titer and volumetric productivity were independent of the degree of cell retention when the total dilution was held constant. When cells were maintained at a low specific growth rate, the product titer was independent of dilution rate and the volumetric productivity increased with increasing dilution rate, again in agreement with mathematical predictions. Since the partially-closed bioreactor could be operated at dilution rates in excess of the maximum specific cellular growth rate, volumetric productivities were greater than those achievable in the open bioreactor. However, when cells were maintained at a high specific growth rate, cell accumulation was limited and product titers decreased at high dilution rates. Therefore, the volumetric productivity in this latter case did not increase at higher dilution rates.     

Continuous cultivation of Hydrogenobacter thermophilus at low partial pressures of H

Growth of the thermophilic H-oxidizing bacterium Hydrogenobacter thermophilus (ITI 553) was achieved in continuous culture using a gas-lift bioreactor. Although the highest equilibrium cell density was obtained at a dilution rate of 0.05 h, the maximum productivity was obtained at 0.1h. At 0.05 h, the maintainable cell density was 7.10 cells/mL at 2-4% oxygen with a gas flow rate of 0.1vvm. The steady-state cell density increased further with increasing gas flow rates. Maximum specific activity of the peroxidase was obtained at 8% oxygen. The total productivity of the enzyme had its maximum at 6-8% oxygen. Increasing gas flow rates had hardly any effect upon peroxidase specific activity, however, productivity was increased due to the increased cell densities obtained.     

Production of Bacillus thuringiensis spores in total cell retention culture and two-stage continuous culture using an internal ceramic filter system

The production of Bacillus thuringiensis spores was investigated in a bioreactor incorporating a ceramic membrane filter to improve spore concentration and volumetric productivity. Two cultivation methods were used in this study: a total cell retention culture (TCRC), and a two-stage continuous culture with partial cell bleeding. In the TCRC, fed by 50 g/L of glucose, a spore concentration of 1.6 x 10(10) CFU/mL was obtained with a spore percentage of greater than 95% and a maximum cell mass of 82.2 g/L. The volumetric productivity was four times higher than that obtained from batch cultivation. In the two-stage continuous culture with partial cell bleeding spore concentration was strongly dependent on the bleed ratio. The spore concentration of 1.8 x 10(9) CFU/mL and the spore percentage of 70% were obtained at the second stage when a bleed ratio of 0.33 and a dilution rate of 0.23 h(-1) were used. (c) 1993 John Wiley & Sons, Inc.     

Continuous propionic acid production from cheese whey usingin situ spin filter

The potential use of spin filter device to retainPropionibacterium acidipropionici in the bioreactor under continuous mode of fermentation and improve propionic acid productivity, was examined. The yield of propionic acid based on lactose concentration was 51% in batch and 54% in continuous (dilution rate=0.05 h⁻¹) operation. The yield in continuous fermentation with cell retention using spin filter of 10 micron size (dilution rate=0.05 h⁻¹) was even higher at 70% (w/w). The volumetric productivity under batch and continuous mode of operation were 0.312 g L⁻¹ h⁻¹ and 0.718 g L⁻¹ h⁻¹ respectively. Continuous fermentation with cell retention demonstrated even higher volumetric productivities at 0.98 g L⁻¹ h⁻¹ with out clogging problems It could be used for utilization of cheese whey to produce propionic acid at higher yield and productivities.     

Novel,linked bioreactor system for continuous production of biologics

A novel, alternative intensified cell culture process comprised of a linked bioreactor system is presented. An N-1 perfusion bioreactor maintained cells in a highly proliferative state and provided a continuous inoculum source to a second bioreactor operating as a continuous-flow stirred-tank reactor (CSTR). An initial study evaluated multiple system steady-states by varying N-1 steady-state viable cell densities, N-1 to CSTR working volume ratios, and CSTR dilution rates. After identifying near optimum system steady-state parameters yielding a relatively high volumetric productivity while efficiently consuming media, a subsequent lab-scale experiment demonstrated the startup and long-term operation of the envisioned manufacturing process for 83 days. Additionally, to compensate for the cell-specific productivity loss over time due to cell line instability, the N-1 culture was also replaced with younger generation cells, without disturbing the steady-state of the system. Using the model cell line, the system demonstrated a two-fold volumetric productivity increase over the commercial-ready, optimized fed-batch process.     

Continuous ethanol production from molasses at 45 °C using alginate-immobilized Kluyveromyces marxianus IMB3 in a continuous-flow bioreactor

The thermotolerant, ethanol-producing yeast strain Kluyveromyces marxianus IMB3 was immobilized in calcium alginate and used in a continuous flow bioreactor to produce ethanol from molasses at 45?°C. The molasses was diluted to yield a number of final sugar concentrations and the effect of molasses sugar concentration on ethanol production by the continuous system was examined. Although maximum ethanol concentrations were obtained using sugar concentrations of 140?g/l, within 10?h of introducing the feed to the column bioreactors, those ethanol concentrations subsequently decreased to lower levels over a 48?h period. Examination of viable yeast cell number within the immobilization matrix indicated a dramatic reduction over this time period. At lower molasses concentrations, ethanol production by the continuous flow system remained relatively constant over this time period. In addition, the effect of residence time on ethanol production by the continuous flow bioreactor was examined at a fixed molasses sugar concentration (120?g/l) and a residence time of 0.66?h was found to be optimal on the basis of volumetric productivity. Efficiencies of the continuous flow bioreactor configuration used in these studies ranged from 31–76%.     

Comparative analysis of ethanolic fermentation in two continuous flocculation bioreactors and effect of flocculation additive

Two types of bioreactor using a flocculating strain of Saccharomyces cerevisiae and continuous ethanolic fermentation as model were compared in terms of start-up evolution, overall performance and power costs. Also, the effect of adding to the medium a polymer — Magna Floc LT25 — that increases floc porosity was studied. The main difference between the reactors lies on the system that is used to recycle the flocculated cells — one presents an external loop with mechanically forced recycling and the other has an airlift configuration with an internal loop. During start-up of both bioreactors, no significant differences between the fermentation kinetics were established, either with or without Magna Floc. In the airlift bioreactor no positive effect of the dilution rate on substrate uptake was observed. Concerning ethanol productivity, both systems behave in a similar way. The best ethanol productivity, 12.9 kg/kg/h, was obtained for the airlift system. This value is 7 times higher than in conventional systems and justifies the interest devoted to flocculation bioreactors. The results also indicate that the activity of the cells that are kept inside the airlift bioreactor is higher and compensates its lower cell retention capacity at higher dilution rates. The addition of Magna Floc to the medium causes a reduction on the ethanol yield on glucose for the external loop system, but allows for an increase in the maximal dilution rate for total glucose consumption. Such a behavior is not observed for the airlift system. The analysis of the power cost associated with the operation of the two bioreactors indicates that the differences between them are only relevant at laboratory and pilot scales. However, from an industrial scale point of view the airlift bioreactor is advantageous because no mechanical parts are involved in recycling.     

Immobilization of the slime mould Dictyostelium discoideum for the continuous production of recombinant human antithrombin III

Recombinant vegetative Dictyostelium discoideum cells were immobilized inside a porous matirx by an inorganic membrane that was permeable to nutrients but not to cells, in order to produce recombinant human antithrombin III. Cells so entrapped could reach up to 15 times higher biomass densities compared with organisms growing freely in suspension. The high cell concentration maintained in the immobilized cell bioreactor caused an increase in specific and volumetric productivity. In continuous operation a maximum volumetric antithrombin productivity of 56 ng h ^–1 ml ^–1 catalyst bulk volume was attained at a dilution rate of 0.016 h ^–1. In addition, the good retention of metabolic activity for several weeks as well as the convenient form of storage and regeneration of the catalytic system were shown. Correspondence to: H. Tiltscher     

Scale-up of virus-like particles production: effects of sparging, agitation and bioreactor scale on cell growth, infection kinetics and productivity

The baculovirus-insect cells expression system was used for the production of self-forming Porcine parvovirus (PPV) like particles (virus-like particles, VLPs) in serum-free medium. At 2l bioreactor scale an efficient production was achieved by infecting the culture at a concentration of 1.5 x 10(6)cells/ml using a low multiplicity of infection of 0.05 pfu per cell. In a continuous bioreactor, it was shown that the uninfected insect cells were not sensitive to local shear stress values up to 2.25 N/m2 at high Reynolds numbers (1.5 x 10(4)) in sparging conditions. Uninfected insect cells can be grown at scaled-up bioreactor at high agitation and sparging rates as long as vortex formation is avoided and bubble entrapment is minimized. An efficient process scale-up to 25 l bioreactor was made using constant shear stress criteria for scale-up. The kinetics of baculovirus infection at low multiplicity of infection, either at different cell concentration or at different scales, are very reproducible, despite the different turbulence conditions present in the bioreactor milieu. The results suggest that the infection kinetics is controlled by the rate of baculovirus-cell receptor attachment and is independent of the bioreactor hydrodynamic conditions. Furthermore, the achieved specific and volumetric productivities were higher at the 25 l scale when compared to the smaller scale bioreactor. Different rates of cell lysis after infection were observed and seem to fully explain both the shift in optimal harvest time and the increase in cell specific productivity. The results emphasize the importance of integrated strategies and engineering concepts in process development at bioreactor stage with the baculovirus insect cell system.     

Modeling methodology for defining a priori the hydrodynamics of a dynamic suspension bioreactor. Application to human induced pluripotent stem cell culture

Three-dimensional dynamic suspension is becoming an effective cell culture method for a wide range of bioprocesses, with an increasing number of bioreactors proposed for this purpose. The complex hydrodynamics establishing within these devices affects bioprocess outcomes and efficiency, and usually expensive in vitro trial-and-error experiments are needed to properly set the working parameters.Here we propose a methodology to define a priori the hydrodynamic working parameters of a dynamic suspension bioreactor, selected as a test case because of the complex hydrodynamics characterizing its operating condition. A combination of computational and analytical approaches was applied to generate operational guideline graphs for defining a priori specific working parameters. In detail, 43 simulations were performed under pulsed flow regime to characterize advective transport within the device depending on different operative conditions, i.e., culture medium flow rate and its duty cycle, cultured particle diameter, and initial particle suspension volume. The operational guideline graphs were then used to set specific hydrodynamic working parameters for an in vitro proof-of-principle test, where human induced pluripotent stem cell (hiPSC) aggregates were cultured for 24 h within the bioreactor. The in vitro findings showed that, under the selected pulsed flow regime, sedimentation was avoided, hiPSC aggregate circularity and viability were preserved, and culture heterogeneity was reduced, thus confirming the appropriateness of the a priori method. This methodology has the potential to be adaptable to other dynamic suspension devices to support experimental studies by providing in silico-based a priori knowledge, useful to limit costs and to optimize culture bioprocesses.     

A new process for the continuous production of succinic acid from glucose at high yield, titer, and productivity

A novel three stages continuous fermentation process for the bioproduction of succinic acid at high concentration, productivity and yield using A. succiniciproducens was developed. This process combined an integrated membrane-bioreactor-electrodialysis system. An energetic characterization of A. succiniciproducens during anaerobic cultured in a cell recycle bioreactor was done first. The very low value of Y(ATP) obtained suggests that an ATP dependent mechanism of succinate export is present in A. succiniciproducens. Under the best culture conditions, biomass concentration and succinate volumetric productivity reach values of 42 g/L and 14.8 g/L.h. These values are respectively 28 and 20 times higher compared to batch cultures done in our laboratory. To limit end-products inhibition on growth, a mono-polar electrodialysis pilot was secondly coupled to the cell recycle bioreactor. This system allowed to continuously remove succinate and acetate from the permeate and recycle an organic acids depleted solution in the reactor. The integrated membrane-bioreactor-electrodialysis process produced a five times concentrated succinate solution (83 g/L) compared to the cell recycle reactor system, at a high average succinate yield of 1.35 mol/mol and a slightly lower volumetric productivity of 10.4 g/L.h. The process combined maximal production yield to high productivity and titer and could be economically viable for the development of a biological route for succinic acid production.     

Effect of particle loading on GM-CSF production by Saccharomyces cerevisiae in a three-phase fluidized bed bioreactor

Continuous production of a recombinant murine granulocyte-macrophage colony-stimulating factor (MuGM-CSF) by immobilized yeast cells, Saccharomyces cerevisiae strain XV2181 (a/a, Trp1) containing plasmid palphaADH2, in a fluidized bed bioreactor was studied at a 0.03 h(-1) dilution rate and various particle loading rates ranging from 5% to 33% (v/v). Cells were immobilized on porous glass beads fluidized in an air-lift draft tube bioreactor. A selective medium containing glucose was used to start up the reactor. After reaching a stable cell concentration, the reactor feed was switched to a rich, nonselective medium containing ethanol as the carbon source for GM-CSF production. GM-CSF production increased initially and then dropped gradually to a stable level. During the same period, the fraction of plasmid-carrying cells declined continuously to a lower level, depending on the particle loading. The relatively stable GM-CSF production, despite the large decline in the fraction of plasmid-carrying cells, was attributed to cell immobilization. As the particle loading rate increased, the plasmid stability also increased. Also, as the particle loading increased from 5% to 33%, total cell density in the bioreactor increased from 16 to 36 g/L, and reactor volumetric productivity increased from 0.36 to 1.31 mg/L.h. However, the specific productivity of plasmid-carrying cells decreased from 0.55 to 0.07 mg/L.g cell. The decreased specific productivity at higher particle loading rates was attributed to reduced growth efficiency caused by nutrient limitations at higher cell densities. Both the reactor productivity and specific cell productivity increased by two- to threefold or higher when the dilution rate was increased from 0.03 to 0.07 h(-1). (c) 1996 John Wiley & Sons, Inc.     

Inclined sedimentation for selective retention of viable hybridomas in a continuous suspension bioreactor.

The continuous separation of nonviable hybridoma cells from viable hybridoma cells by using a narrow rectangular channel that is inclined from the vertical has been investigated experimentally. The effectiveness of the settler in selectively retaining viable hybridomas in the bioreactor while permitting the removal of nonviable hybridomas has been shown to depend on the flow rate through the settler. Intermediate flow rates through the settler have been found to provide the highest removal of nonviable hybridomas relative to viable hybridoma retention. At high dilution rates through the chemostat, over 95% of the viable cells could be partitioned to the bottom of the settler while over 50% of the nonviable cells are removed through the top of the settler. This successful separation is due to the significantly larger size of the viable hybridomas than the nonviable ones. A continuous perfusion experiment was performed in which an external inclined settler was used to retain virtually all of the viable hybridomas in the culture, while selectively removing from the culture approximately 20% of the nonviable cells that entered the settler. A stable viable cell concentration of 1.0 x 10(7) cells/mL was achieved, as was an antibody productivity of over 50 micrograms/(mL.day). These represent 3- and 6-fold increases, respectively, over the values obtained from a chemostat culture without cell retention.     

Continuous production of 1,3-propanediol using raw glycerol with immobilized Clostridium beijerinckii NRRL B-593 in comparison to suspended culture

The continuous production of 1,3-propanediol (1,3-PDO) was investigated with Clostridium beijerinckii NRRL B-593 using raw glycerol without purification obtained from a biodiesel production process. Ceramic rings and pumice stones were used for cell immobilization in a packed-bed bioreactor. For comparison purpose, a control bioreactor with suspended culture was also run. The effect of hydraulic retention time (HRT) on the production of 1,3-PDO in both immobilized and suspended bioreactors were also investigated. The study revealed that HRT is an important factor for both immobilized and suspended systems and a HRT of 2 h is the best one in terms of volumetric production rate (g 1,3-PDO/L/h). Furthermore, cell immobilization had also obvious benefits especially for the robustness and the reliability of the production. The results indicated that cell immobilization achieved a 2.5-fold higher productivity in comparison to suspended cell system. Based on our results, continuous production of 1,3-PDO with immobilized cells is an efficient method, and raw glycerol can be utilized without any pretreatment.     

Growth and exopolysaccharide production during free and immobilized cell chemostat culture of Lactobacillus rhamnosus RW-9595M

AIMS: Biomass and exopolysaccharide (EPS) production were studied during chemostat cultures in whey permeate medium with Lactobacillus rhamnosus RW-9595M-free cells and cells immobilized on solid porous supports (ImmobaSil). METHODS AND RESULTS: A continuous culture with free cells was conducted for 9 days at dilution rates (D) between 0.3 and 0.8 h(-1) in yeast extract (YE)/mineral supplemented whey permeate. Maximum EPS production (1808 mg l(-1)) and volumetric productivity (542.6 mg l(-1) h(-1)) were obtained for a low D of 0.3 h(-1). A continuous fermentation in a two-stage bioreactor system, composed of a first stage with immobilized cells and a second stage inoculated with free cells produced in the first reactor, was carried out for 32 days. The influence of YE concentration, temperature and dilution rate, and their interactions on biomass, EPS and lactic acid production was investigated. A statistically significant model was found only for lactic acid production. Marked cell morphological and physiological changes led to the formation of very large cell-containing aggregates and a low mean soluble EPS production (138 mg l(-1)). Aggregate volumetric productivity of the two-stage system varied between 5.7 and 49.5 g l(-1) h(-1) for different fermentation conditions and times. Aggregates contained a very high biomass concentration, estimated at 74% of aggregate dry weight by nitrogen analysis and 4.3 x 10(12) CFU g(-1) by a DNA extraction method and a high nonsoluble polysaccharide content (14.2%). At age 24 days, insoluble EPS concentration and volumetric productivity were 1250 mg l(-1) and 2240 mg l(-1) h(-1) respectively. The physiological changes were shown to be reversible when cells were incubated during three successive batch cultures. CONCLUSIONS: EPS production and volumetric productivity during continuous free-cell chemostat cultures with L. rhamnosus RW-9595M are among the highest values reported for lactobacilli in literature. Immobilization and continuous culture resulted in low soluble EPS production and large morphological and physiological changes of L. rhamnosus RW-9595M, with formation of macroscopical aggregates mainly composed of biomass and nonsoluble EPS. SIGNIFICANCE AND IMPACT OF THE STUDY: This is the first study on continuous EPS production by immobilized LAB. Immobilization and culture time-induced cell aggregation and could be used to produce new synbiotic products with very high viable cell and EPS concentrations.     

Efficient and reproducible mammalian cell bioprocesses without probes and controllers?

Bioprocesses for recombinant protein production with mammalian cells are typically controlled for several physicochemical parameters including the pH and dissolved oxygen concentration (DO) of the culture medium. Here we studied whether these controls are necessary for efficient and reproducible bioprocesses in an orbitally shaken bioreactor (OSR). Mixing, gas transfer, and volumetric power consumption (P(V)) were determined in both a 5-L OSR and a 3-L stirred-tank bioreactor (STR). The two cultivation systems had a similar mixing intensity, but the STR had a lower volumetric mass transfer coefficient of oxygen (k(L)a) and a higher P(V) than the OSR. Recombinant CHO cell lines expressing either tumor necrosis factor receptor as an Fc fusion protein (TNFR:Fc) or an anti-RhesusD monoclonal antibody were cultivated in the two systems. The 5-L OSR was operated in an incubator shaker with 5% CO(2) in the gas environment but without pH and DO control whereas the STR was operated with or without pH and DO control. Higher cell densities and recombinant protein titers were obtained in the OSR as compared to both the controlled and the non-controlled STRs. To test the reproducibility of a bioprocess in a non-controlled OSR, the two CHO cell lines were each cultivated in parallel in six 5-L OSRs. Similar cell densities, cell viabilities, and recombinant protein titers along with similar pH and DO profiles were achieved in each group of replicates. Our study demonstrated that bioprocesses can be performed in OSRs without pH or DO control in a highly reproducible manner, at least at the scale of operation studied here.     

Continuous ethanol production from Jerusalem artichoke tubers. II. Use of immobilized cells of Kluyveromyces marxianus

Kluyveromyces marxianus UCD (FST) 55-82 cells were immobilized in Na alginate beads and used in a packed-bed bioreactor system for the continuous production of ethanol from the extract of Jerusalem artichoke tubers. Volumetric ethanol productivities of 104 and 80 g ethanol/ L/h were obtained at 80 and 92% sugar utilization, respectively. The maximum volumetric ethanol productivity of the immobilized cell bioreactor system was found to be 15 times higher than that of an ordinary-stirred-tank (CST) bioreactor using cells of K. marxianus. The immobilized cell bioreactor system was operated continuously at a constant dilution rate of 0.66 h(-1) for 12 days resulting in only an 8% loss of the original immobilized cell activity, which corresponds to an estimated half-life of ca. 72 days. The maximum specific ethanol productivity and maximum specific sugar uptake rate of the immobilized cells were found to be 0.55 g ethanol/g/biomass/h and 1.21 g sugars/g biomass/h, respectively.     

High production of 1,3-propanediol from industrial glycerol by a newly isolated Clostridium butyricum strain

Batch and continuous cultures of a newly isolated Clostridium butyricum strain were carried out on industrial glycerol, the major by-product of the bio-diesel production process. For both types of cultures, the conversion yield obtained was around 0.55 g of 1,3-propanediol formed per 1 g of glycerol consumed whereas the highest 1,3-propanediol concentration, achieved during the single-stage continuous cultures was 35-48 g l-1. Moreover, the strain presented a strong tolerance at the inhibitory effect of the 1,3-propanediol, even at high concentrations of this substance at the chemostat (e.g. 80 g l-1). 1,3-Propanediol was associated with cell growth whereas acetate and butyrate seemed non growth-associated products. At low and medium dilution rates (until 0.1 h-1), butyrate production was favoured, whereas at higher rates acetate production increased. The maximum 1,3-propanediol volumetric productivity obtained was 5.5 g l-1 h-1. A two-stage continuous fermentation was also carried out. The first stage presented high 1,3-propanediol volumetric productivity, whereas the second stage (with a lower dilution rate) served to further increase the final product concentration. High 1,3-propanediol concentrations were achieved (41-46 g l-1), with a maximum volumetric productivity of 3.4 g l-1 h-1. A cell concentration decrease was reported between the second and the first fermentor.     

Physiological heterogeneity of Pseudomonas taetrolens during lactobionic acid production

Physiological heterogeneity constitutes a critical parameter in biotechnological systems since both metabolite yield and productivity are often hampered by the presence of undesired physiological cell subpopulations. In the present study, the physiological status and functionality of Pseudomonas taetrolens cells were monitored by multiparameter flow cytometry during fermentative lactobionic acid production at the shake-flask and bioreactor scale. In shake-flask fermentation, the onset of the lactobionic acid production phase was accompanied by a progressive loss of cellular metabolic activity, membrane polarization, and membrane integrity concomitantly to acidification. In fact, population dynamics has shown the prevalence of damaged and dead subpopulations when submitted to a pH?<?4 from 16?h onwards. Furthermore, fluorescence-activated cell sorting revealed that these sublethally injured cells were nonculturable. In contrast, P. taetrolens cells exhibited a robust physiological status during bioreactor cultivations performed with a pH-shifted strategy at 6.5, remaining predominantly healthy and metabolically active (>96?%) as well as maintaining bioconversion efficiency throughout the course of the fermentation. Additionally, an assessment of the seed culture’s physiological robustness was carried out in order to determine the best seed culture age. Results showed that bioreactor culture performance, growth, and lactobionic acid production efficiency were strongly dependent on the physiological heterogeneity displayed by the seed culture. This study provides the most suitable criteria for optimizing lactobionic acid production efficiency through a novel flow cytometric-based approach based on the physiological status of P. taetrolens. It also constitutes a valuable, broad-ranging methodology for the enhancement of microbial bioprocesses involved in the production of secondary metabolites.     

Uptake and turnover of acetate in hypersaline environments

Abstract: Acetate uptake and turnover rates were determined for the heterotrophic community in hypersaline environments (saltern crystallizer ponds, the Dead Sea) dominated by halpphilic Archaea. Acetate was formed from glycerol, which is potentially the major available carbon source for natural communities of halophilic Archaea. Values of [ K _t+ S _n] (the sum of the substrate affinity and the substrate concentration present in situ) for acetate measured in saltern crystallizer ponds were around 4.5–11.5 μM, while in the Dead Sea during a Dunaliella bloom values up to 12.8 μM were found. Maximal theoretical rates ( V _max) of acetate uptake in saltern crystallizer ponds were 12–56 nmol l⁻¹ h⁻¹, with estimated turnover times for acetate ( T _t) between 127–730 h at 35°C. V _max values measured in the Dead Sea were between 0.8 and 12.8 nmol l⁻¹ h⁻¹, with turnover times in the range of 320–2190 h. V _max values for acetate were much lower than those for glycerol. Comparisons with pure cultures of halophilic Archaea grown under different conditions showed that the natural communities were not adapted for preferential use of acetate. Both in natural brines and in pure cultures of halophilic Archaea, acetate incorporation rates rapidly decreased above the optimum pH value, probably since acetate enters the cell only in its unionized form. The low affinity for acetate, together with low potential utilization rates result in the long acetate turnover times, which explains the accumulation of acetate observed when low concentrations of glycerol are supplied as a nutrient to natural communities of halophilic Archaea.