Phosphorus-31 and carbon-13 nuclear magnetic resonance studies of glucose and xylose metabolism in cell suspensions and agarose-immobilized cultures of Pichia stipitis and Saccharomyces cerevisiae.

The metabolism of glucose and xylose as a function of oxygenation in Pichia stipitis and Saccharomyces cerevisiae cell suspensions was studied by 31P and 13C nuclear magnetic resonance spectroscopy. The rate of both glucose and xylose metabolism was slightly higher and the production of ethanol was slightly lower in aerobic than in anoxic cell suspensions of P. stipitis. As well, the cytoplasmic pH of oxygenated cells was more alkaline than that of nonoxygenated cells. In contrast, in S. cerevisiae, the intracellular pH and the rate of glucose metabolism and ethanol production were the same under aerobic and anoxic conditions. Agarose-immobilized Pichia stipitis was able to metabolize xylose or glucose for 24 to 60 h at rates and with theoretical yields of ethanol similar to those obtained with anoxic cell suspensions. Cell growth within the beads, however, was severely compromised. The intracellular pH [pH(int)] of the entrapped cells fell to more acidic pH values in the course of the perfusions relative to corresponding cell suspensions. Of importance was the observation that no enhancement in the rate of carbohydrate metabolism occurred in response to changes in the pH(int) value. In contrast to P. stipitis, agarose-immobilized Saccharomyces cerevisiae showed a dramatic twofold increase in its ability to metabolize glucose in the immobilized state relative to cell suspensions. This strain was also able to grow within the beads, although the doubling time for the entrapped cells was longer, by a factor of 2, than the value obtained for log-phase batch cultures. Initially, the pH(int) of the immobilized cells was more alkaline than was observed with the corresponding S. cerevisiae cell suspensions; however, over time, the intracellular pH became increasingly acidic. As with immobilized P. stipitis, however, the pH(int) did not play a key role in controlling the rate of glucose metabolism.     

Phosphorus-31 and carbon-13 nuclear magnetic resonance studies of glucose and xylose metabolism in Candida tropicalis cell suspensions.

The metabolism of glucose and xylose was studied as a function of oxygenation in suspensions of Candida tropicalis by 31P and 13C nuclear magnetic resonance spectroscopy. Both the rate of carbohydrate metabolism and the cytoplasmic pH were independent of the rate of oxygenation in cells metabolizing glucose. However, these two parameters were markedly dependent on the rate of oxygenation in C. tropicalis cells metabolizing xylose. For example, the cytoplasmic pH in fully oxygenated xylose-metabolizing cells was 7.8 but decreased to 6.3 in anoxic cells. In general, suspensions of cells consuming xylose had a lower rate of sugar uptake, a more acidic cytoplasmic pH, lower levels of sugarphosphomonoesters (SP) and ATP, higher levels of intracellular Pi, a more alkaline vacuolar pH, and a lower rate of extracellular Pi assimilation and polyphosphate synthesis than cells consuming glucose. These observations indicate that C. tropicalis metabolizing xylose is less energized than glucose-metabolizing cells. On both carbon sources, however, an inverse correlation between intracellular levels of SP and Pi was observed. Also, uptake of extracellular Pi correlated with the synthesis of polyphosphates within the cells. During anoxia, Pi was not taken up, and polyphosphates were hydrolyzed instead to fulfill the cells' requirements for phosphate.     

热带假丝酵母XYL1在Pichia pastoris中的表达及固定化细胞发酵生产木糖醇

利用克隆获得的具有双重辅酶依赖性的热带假丝酵母xyl1基因,通过表达载体pGAPZB转入巴斯德毕赤酵母X-33,采用海藻酸钙凝胶包埋法固定该重组菌,研究固定化条件下玉米芯水解液的发酵特性,实现对玉米芯等农业废弃物资源的利用。结果表明,转化xyl1基因的巴斯德毕赤酵母X-33的总酶活达到1.64U/mg。固定化细胞的最适发酵条件为pH 6.0、30℃、接种量20%、装液量28%、转速130r/min,木糖醇转化率为37.5%。为生物转化法大规模生产木糖醇以及乙醇提供新的选择途径。     

Measurement and analysis of intracellular ATP levels in metabolically engineered Zymomonas mobilis fermenting glucose and xylose mixtures

Intracellular adenosine-5'-triphosphate (ATP) levels were measured in a metabolically engineered Zymomonas mobilis over the course of batch fermentations of glucose and xylose mixtures. Fermentations were conducted over a range of pH (5-6) in the presence of varying initial amounts of acetic acid (0-8 g/L) using a 10% (w/v) total sugar concentration (glucose only, xylose only, or 5% glucose/5% xylose mixture). Over the design space investigated, ethanol process yields varied between 56.6% and 92.3% +/- 1.3% of theoretical, depending upon the test conditions. The large variation in process yields reflects the strong effect pH plays in modulating the inhibitory effect of acetic acid on fermentation performance. A corresponding effect was observed on maximum cellular specific growth rates, with the rates varying between a low of 0.15 h(-1) observed at pH 5 in the presence of 8 g/L acetic acid to a high of 0.32 +/- 0.02 h(-1) obtained at pH 5 or 6 when no acetic acid was initially present. While substantial differences were observed in intracellular specific ATP concentration profiles depending upon fermentation conditions, maximum intracellular ATP accumulation levels varied within a relatively narrow range (1.5-3.8 mg ATP/g dry cell mass). Xylose fermentations produced and accumulated ATP at much slower rates than mixed sugar fermentations (5% glucose, 5% xylose), and the ATP production and accumulation rates in the mixed sugar fermentations were slightly slower than in glucose fermentations. Results demonstrate that higher levels of acetic acid delay the onset and influence the extent of intracellular ATP accumulation. ATP production and accumulation rates were most sensitive to acetic acid at lower values of pH.     

Controlled transient changes reveal differences in metabolite production in two<Emphasis Type="Italic"> Candida</Emphasis> yeasts

Physiological responses during growth on xylose and the xylose-degrading pathway of Candida tropicalis and Candida guilliermondii yeasts were investigated. The responses to a linearly decreasing oxygen transfer rate and a simultaneously increasing dilution rate were compared. C. guilliermondii produced acetate but no ethanol, and C. tropicalis ethanol but no acetate under oxygen limitation. Both strains produced glycerol. The D-xylose reductase of C. guilliermondii is exclusively NADPH-dependent. and acetate production regenerated NADPH. The xylose'reductase of C. tropicalis has a dual dependency for both NADH and NADPH. It regenerated NAD by producing ethanol. Both strains regenerated NAD by producing glycerol. The effect of intracellular NADH accumulation to xylose uptake and metabolite production was studied by using formate as a cosubstrate. Formate feeding in C. tropicalis triggered the accumulation of glycerol, ethanol and xylitol. Consequently, the specific xylose consumption increased 28% during formate feeding, from 477 to 609 C-mmol/C-mol cell dry-weight (CDW)/h. In C. guilliermondii cultures. formate feeding resulted only in glycerol accumulation. The specific xylose consumption increased 6%, from 301 to 319 C-mmol/C-mol CDW/h, until glycerol started to accumulate.     

Fermentation of xylose and rice straw hydrolysate to ethanol byCandida shehatae NCL-3501

Candida shehatae NCL-3501 utilized glucose and xylose efficiently in batch cultures. The specific rate of ethanol production was higher with mixtures of glucose and xylose (0.64–0.83 g g^–1 cells d^–1) compared to that with individual sugars (0.38–0.58 g g^–1 cells d^–1). Although the optimum temperature for growth was 30°C, this strain grew and produced appreciable levels of ethanol at 45°C. A stable ethanol yield (0.40–0.43 g g^–1 substrate utilized) was obtained between 10 g L^–1 and 80 g L^–1 of initial xylose concentration. Conversion efficiency was further improved by immobilization of the cells in calcium alginate beads. Free or immobilized cells ofC. shehatae NCL-3501 efficiently utilized sugars present in rice straw hemicellulose hydrolysate, prepared by two different methods, within 48 h. Ethanol yields of 0.45 g g^–1 and 0.5 g g^–1 from autohydrolysate, and 0.37 g g^–1 from acid hydrolysate were produced by free and immobilized cells, respectively.     

31P nuclear magnetic resonance study of the effect of azide on xylose fermentation by Candida tropicalis.

Maximal ethanol production by Candida tropicalis grown on xylose was obtained at an oxygen transfer rate of 5 to 7 mmol/liter per h. Addition of 0.2 mM azide increased the ethanol yield by a factor of 3 to 4, based on the cell mass produced, and decreased the formation of the by-product xylitol by 80%. In the presence of azide, ethanol was reassimilated before the carbon source was depleted. At all oxygenation levels studied, azide caused 25 to 60% of the carbon to be lost, most probably as carbon dioxide. Identical spectra were obtained with 31P nuclear magnetic resonance spectroscopy performed on extracts of C. tropicalis grown on xylose in the absence and presence of azide. Azide lowered the levels of sugar phosphates. Enzymatic analysis showed extremely low levels of fructose 1,6-diphosphate compared with the levels obtained in the absence of azide, while the level of malate, a citric acid cycle intermediate, was not influenced by azide. 31P nuclear magnetic resonance spectroscopy performed on xylose-grown whole cells of C. tropicalis showed that azide lowered the intracellular pH, inhibited the uptake of external Pi, and decreased the buildup of polyphosphate in relation to results with untreated cells. Similar results were obtained with the uncoupler of oxidative phosphorylation carbonyl cyanide m-chlorophenylhydrazone (CCCP), except that CCCP treatment led to extremely high levels of internal Pi. The dual effect of azide as a respiratory inhibitor and as an uncoupler is discussed with respect to the metabolism and product formation in xylose-assimilating C. tropicalis.     

31P nuclear magnetic resonance study of the effect of azide on xylose fermentation by Candida tropicalis

Maximal ethanol production by Candida tropicalis grown on xylose was obtained at an oxygen transfer rate of 5 to 7 mmol/liter per h. Addition of 0.2 mM azide increased the ethanol yield by a factor of 3 to 4, based on the cell mass produced, and decreased the formation of the by-product xylitol by 80%. In the presence of azide, ethanol was reassimilated before the carbon source was depleted. At all oxygenation levels studied, azide caused 25 to 60% of the carbon to be lost, most probably as carbon dioxide. Identical spectra were obtained with 31P nuclear magnetic resonance spectroscopy performed on extracts of C. tropicalis grown on xylose in the absence and presence of azide. Azide lowered the levels of sugar phosphates. Enzymatic analysis showed extremely low levels of fructose 1,6-diphosphate compared with the levels obtained in the absence of azide, while the level of malate, a citric acid cycle intermediate, was not influenced by azide. 31P nuclear magnetic resonance spectroscopy performed on xylose-grown whole cells of C. tropicalis showed that azide lowered the intracellular pH, inhibited the uptake of external Pi, and decreased the buildup of polyphosphate in relation to results with untreated cells. Similar results were obtained with the uncoupler of oxidative phosphorylation carbonyl cyanide m-chlorophenylhydrazone (CCCP), except that CCCP treatment led to extremely high levels of internal Pi. The dual effect of azide as a respiratory inhibitor and as an uncoupler is discussed with respect to the metabolism and product formation in xylose-assimilating C. tropicalis.     

Production of butanol from glucose and xylose with immobilized cells of Clostridium acetobutylicum

Pretreated cotton towels were used as carriers to immobilize Clostridium acetobutylicum CGMCC 5234 cells for butanol or ABE production from glucose and xylose. Results showed that cell immobilization was a promising method to increase butanol concentration, yield and productivity regardless of the sugar sources compared with cell suspension. In this study, a high butanol concentration of 10.02 g/L with a yield of 0.20 g/g was obtained from 60 g/L xylose with 9.9 g/L residual xylose using immobilized cells compared with 8.48 g/L butanol and a yield of 0.141 g/g with 20.2 g/L residual xylose from 60 g/L xylose using suspended cells. In mixed-sugar fermentation (30 g/L glucose plus 30 g/L xylose), the immobilized cultures produced 11.1 g/L butanol with a yield of 0.190 g/g, which were 28.3% higher than with suspended cells (8.65 g/L) during which 30 g/L glucose was utilized completely using both immobilized and suspended cells while 3.46 and 13.1 g/L xylose maintained untilized for immobilized and suspended cells, respectively. Based on the results, we speculated that immobilized cells showed enhanced tolerance to butanol toxicity and the cultures preferred glucose to xylose during ABE fermentation. Moreover, the cultures showed obvious difference when grown between high initial concentrations of glucose and those of xylose. Repeated-batch fermentations from glucose with immobilized cells showed better long-term stability than from xylose. At last, the morphologies of free and immobilized cells adsorbed on pretreated cotton towels during the growth cycle were examined by SEM.     

Immobilization of Nicotiana tabacum plant cell suspensions within calcium alginate gel beads for the production of enhanced amounts of scopolin

Scopolin-producing cells of Nicotiana tabacum were immobilized within Ca-alginate gel beads. Free cell suspensions accumulated scopolin within cytoplasmic compartments and cell disruption was necessary to recover scopolin. On the contrary, immobilized plant cells excreted considerable amounts of scopolin. Scopolin diffused throughout the gel matrix and reached the culture media. A large fraction of produced scopolin could then be recovered from the culture medium without disrupting cells. Immobilized N. tabacum cells produced more scopolin than free cell suspensions did (3.8 mg/g fresh weight biomass [into the culture media] versus 0.2 mg/g fresh weight biomass [intracellular]). Variation of the immobilization conditions revealed a marked influence on the behavior of N. tabacum plant cells: production of scopolin and enhanced excretion, cell growth, and morphological aspect of plant cell colonies. This excretion phenomenon could be used advantageously at an industrial production level.     

Comparison of suspended and immobilized yeast metabolism using 31P nuclear magnetic resonance spectroscopy

Summary ³¹P nuclear magnetic resonance has been employed to monitor noninvasively Saccharomyces cerevisiae anaerobic glucose metabolism in suspended and immobilized cells. Results show that cell entrapment in Ca-alginate beads alters cell metabolism compared to that in suspended cells. Assuming similar intracellular ionic strength, differences in intracellular phosphate chemical shift indicate that the internal pH of the immobilized cells is lower than the suspended cell internal pH. This result is consistent with higher ethanol production rates exhibited by immobilized yeast.     

Application of a compatible xylose isomerase in simultaneous bioconversion of glucose and xylose to ethanol

Simultaneous isomerisation and fermentation (SIF) of xylose and simultaneous isomerisation and cofermentation (SICF) of glucose-xylose mixture was carried out by the yeastSaccharomyces cerevisiae in the presence of a compatible xylose isomerase. The enzyme converted xylose to xylulose andS. cerevisiae fermented xylulose, along with glucose, to ethanol at pH 5.0 and 30°C. This compatible xylose isomerase fromCandida boidinii, having an optimum pH and temperature range of 4.5–5.0 and 30–50°C respectively, was partially purified and immobilized on an inexpensive, inert and easily available support, hen egg shell. An immobilized xylose isomerase loading of 4.5 IU/(g initial xylose) was optimum for SIF of xylose as well as SICF of glucose-xylose mixture to ethanol byS. cerevisiae. The SICF of 30 g/L glucose and 70 g xylose/L gave an ethanol concentration of 22.3 g/L with yield of 0.36 g/(g sugar consumed) and xylose conversion efficiency of 42.8%.     

Influence of polymolecular events on inactivation behavior of xylose isomerase from Thermotoga neapolitana 5068

The inactivation behavior of the xylose isomerase from Thermotoga neapolitana (TN5068 XI) was examined for both the soluble and immobilized enzyme. Polymolecular events were involved in the deactivation of the soluble enzyme. Inactivation was biphasic at 95 degrees C, pH 7.0 and 7.9, the second phase was concentration-dependent. The enzyme was most stable at low enzyme concentrations, however, the second phase of inactivation was 3- to 30-fold slower than the initial phase. Both phases of inactivation were more rapid at pH 7.9, relative to 7.0. Differential scanning calorimetry of the TN5068 XI revealed two distinct thermal transitions at 99 degrees and 109 degrees C. The relative magnitude of the second transition was dramatically reduced at pH 7.9 relative to pH 7.0. Approximately 24% and 11% activity were recoverable after the first transition at pH 7.0 and 7.9, respectively. When the TN5068 XI was immobilized by covalent attachment to glass beads, inactivation was monophasic with a rate corresponding to the initial phase of inactivation for the soluble enzyme. The immobilized enzyme inactivation rate corresponded closely to the rate of ammonia release, presumably from deamidation of labile asparagine and/or glutamine residues. A second, slower inactivation phase suggests the presence of an unfolding intermediate, which was not observed for the immobilized enzyme. The concentration dependence of the second phase of inactivation suggests that polymolecular events were involved. Formation of a reversible polymolecular aggregate capable of protecting the soluble enzyme from irreversible deactivation appears to be responsible for the second phase of inactivation seen for the soluble enzyme. Whether this characteristic is common to other hyperthermophilic enzymes remains to be seen.     

Xylose isomerase improves growth and ethanol production rates from biomass sugars for both Saccharomyces pastorianus and Saccharomyces cerevisiae

The demand for biofuel ethanol made from clean, renewable nonfood sources is growing. Cellulosic biomass, such as switch grass (Panicum virgatum L.), is an alternative feedstock for ethanol production; however, cellulosic feedstock hydrolysates contain high levels of xylose, which needs to be converted to ethanol to meet economic feasibility. In this study, the effects of xylose isomerase on cell growth and ethanol production from biomass sugars representative of switch grass were investigated using low cell density cultures. The lager yeast species Saccharomyces pastorianus was grown with immobilized xylose isomerase in the fermentation step to determine the impact of the glucose and xylose concentrations on the ethanol production rates. Ethanol production rates were improved due to xylose isomerase; however, the positive effect was not due solely to the conversion of xylose to xylulose. Xylose isomerase also has glucose isomerase activity, so to better understand the impact of the xylose isomerase on S. pastorianus, growth and ethanol production were examined in cultures provided fructose as the sole carbon. It was observed that growth and ethanol production rates were higher for the fructose cultures with xylose isomerase even in the absence of xylose. To determine whether the positive effects of xylose isomerase extended to other yeast species, a side-by-side comparison of S. pastorianus and Saccharomyces cerevisiae was conducted. These comparisons demonstrated that the xylose isomerase increased ethanol productivity for both the yeast species by increasing the glucose consumption rate. These results suggest that xylose isomerase can contribute to improved ethanol productivity, even without significant xylose conversion.     

Biosorption of Cr (VI) with Trichoderma viride immobilized fungal biomass and cell free Ca-alginate beads

Ability of Cr (VI) biosorption with immobilized Trichoderma viride biomass and cell free Ca-alginate beads was studied in the present study. Biosorption efficiency in the powdered fungal biomass entrapped in polymeric matric of calcium alginate compared with cell free calcium alginate beads. Effect of pH, initial metal ion concentration, time and biomass dose on the Cr (VI) removal by immobilized and cell free Ca-alginate beads were also determined. Biosorption of Cr (VI) was pH dependent and the maximum adsorption was observed at pH 2.0. The adsorption equilibrium was reached in 90 min. The maximum adsorption capacity of 16.075 mgg(-1) was observed at dose 0.2 mg in 100 ml of Cr (VI) solution. The high value of kinetics rate constant Kad (3.73 x 10(-2)) with immobilized fungal biomass and (3.75 x 10(-2)) with cell free Ca- alginate beads showed that the sorption of Cr (VI) ions on immobilized biomass and cell free Ca-alginate beads followed pseudo first order kinetics. The experimental results were fitted satisfactory to the Langmuir and Freundlich isotherm models. The hydroxyl (-OH) and amino (-NH) functional groups were responsible in biosorption of Cr (VI) with fungal biomass spp. Trichoderma viride analysed using Fourier Transform Infrared (FTIR) Spectrometer.     

Modeling alcoholic fermentation of glucose/xylose mixtures by ethanologenic Escherichia coli as a function of pH

In order to understand the effect of pH on growth and ethanol production in ethanologenic Escherichia coli, we investigated the kinetic behavior of ethanologenic E. coli during alcoholic fermentation of glucose or xylose in a controlled pH environment and the fermentation of glucose, xylose, or their mixtures without pH control. Based on the Monod equation, an unstructured and unsegregated kinetic model was proposed as a function of the pH of the fermentation medium. The pH effects on cell growth, sugar consumption, and ethanol production were taken into account in the proposed model. Both cell growth and ethanol production were found to be significantly influenced by the pH of the fermentation medium. The optimal pH range for ethanol production by ethanologenic E. coli on either glucose or xylose was 6.0–6.5. The highest value of the maximum specific growth rate (μ _m) was obtained at pH 7.0. In the kinetic model of the fermentations of the sugar mixture, two inhibition terms related to glucose concentrations were included in both the cell growth and ethanol production equations because of the strong inhibitions of glucose and glucose metabolites on xylose metabolism. A good fit was found between model predictions and experimental data for both single-sugar and mixed-sugar fermentations without pH control within the experimental domain.     

Characterization of Thermoanaerobacter Glucose Isomerase in Relation to Saccharidase Synthesis and Development of Single-Step Processes for Sweetener Production

Regulation of glucose isomerase synthesis was studied in Thermoanaerobacter strain B6A, which fermented a wide variety of carbohydrates including glucose, xylose, lactose, starch, and xylan. Glucogenic amylase activities and β-galactosidase were produced constitutively, whereas the synthesis of glucose isomerase was induced by either xylose or xylan. Production of these saccharidase activities was not significantly repressed by the presence of glucose or 2-deoxyglucose in the growth media. Glucose isomerase production was optimized by controlling the culture pH at 5.5 during xylose fermentation. The apparent temperature and pH optima for these cell-bound saccharidase activities were as follows: glucose isomerase, 80°C, pH 7.0 to 7.5; glucogenic amylase, 70°C, pH 5.0 to 5.5; and β-galactosidase, 60°C, pH 6.0 to 6.5 Glucose isomerase, glucogenic amylase, and β-galactosidase were produced in xylose-grown cells that were active and stable at 60 to 70°C and pH 6.0 to 6.5. Under single-step process conditions, these saccharidase activities in whole cells or cell extracts converted starch or lactose directly into fructose mixtures. A total of 96% of initial liquefied starch was converted into a 49:51 mixture of glucose and fructose, whereas 85% of initial lactose was converted into a 40:31:29 mixture of galactose, glucose, and fructose.     

Xylitol production is increased by expression of codon-optimized Neurospora crassa xylose reductase gene in Candida tropicalis

Xylose reductase (XR) is the first enzyme in D: -xylose metabolism, catalyzing the reduction of D: -xylose to xylitol. Formation of XR in the yeast Candida tropicalis is significantly repressed in cells grown on medium that contains glucose as carbon and energy source, because of the repressive effect of glucose. This is one reason why glucose is not a suitable co-substrate for cell growth in industrial xylitol production. XR from the ascomycete Neurospora crassa (NcXR) has high catalytic efficiency; however, NcXR is not expressed in C. tropicalis because of difference in codon usage between the two species. In this study, NcXR codons were changed to those preferred in C. tropicalis. This codon-optimized NcXR gene (termed NXRG) was placed under control of a constitutive glyceraldehyde-3-phosphate dehydrogenase (GAPDH) promoter derived from C. tropicalis, and integrated into the genome of xylitol dehydrogenase gene (XYL2)-disrupted C. tropicalis. High expression level of NXRG was confirmed by determining XR activity in cells grown on glucose medium. The resulting recombinant strain, LNG2, showed high XR activity (2.86 U (mg of protein)(-1)), whereas parent strain BSXDH-3 showed no activity. In xylitol fermentation using glucose as a co-substrate with xylose, LNG2 showed xylitol production rate 1.44 g L(-1) h(-1) and xylitol yield of 96% at 44 h, which were 73 and 62%, respectively, higher than corresponding values for BSXDH-3 (rate 0.83 g L(-1) h(-1); yield 59%).     

Physiological difference during ethanol fermentation between calcium alginate-immobilized Candida tropicalis and Saccharomyces cerevisiae

Calcium alginate-immobilized Candida tropicalis and Saccharomyces cerevisiae are compared for glucose fermentation. Immobilized C. tropicalis cells showed a slight morphological alteration during ethanol production at 40 degrees C, but their fermentation capacity was reduced by 25%. Under immobilization conditions, the two species demonstrated two different mathematical patterns when the relationship between growth rate, respiration rate, and ethanol tolerance was assessed. The interspecific difference in behavior of immobilized yeast cells is mainly due to their natural metabolic preference. The production of CO(2) by calcium alginate-immobilized C. tropicalis, as well as the lower supply of oxygen to the cells, are the major factors that reduce ethanol production.     

Increasing the stability of immobilizedLactococcus lactis cultures stored at 4 °C

Summary Immobilized cell technology was used to prepare concentrated cultures ofLactococcus lactis that lost only 22% of viability over a 30-day storage period at 4°C. Concentrated cultures ofL lactis CRA-1 were immobilized in calcium alginate beads and added to glycerol, NaCl or sucrose-NaCl solutions in order to obtain a_w readings ranging from 0.91 to 0.97. The suspensions were subsequently placed at 4°C and viability (CFU g^–1 of bead) was followed during storage. Viability losses were high at a_w readings of 0.95 and 0.97 and pH dropped significantly (up to one unit) in the unbuffered solutions. Addition of 1% soytone or glycerophosphate helphed stabilize pH, and a beneficial effect on viability during storage was observed in the glycerol-soytone mix when the beads were added to the conservation solutions immediately following immobilization. When beads were added to the conservation solution immediately following immobilization, a 70% drop in cell counts occurred during the first 5 days of incubation. Dipping theL lactis-carrying beads in milk for 2h before mixing with the glycerolsoytone 0.93 a_w solution reduced this initial 5-day viability loss. Cultures grown in the alginate beads also had good stability in the 0.93 a_w glycerol-soytone solution, where 78% of the population was viable after 30 days at 4°C. The process could be used to store immobilized cells at a processing plant, or by suppliers of lactic starters who wish to ship cultures without freezing or drying.