Enhanced hydrogen production from glucose using ldh- and frd-inactivated Escherichia coli strains

We improved the hydrogen yield from glucose using a genetically modified Escherichia coli. E. coli strain SR15 (ΔldhA, ΔfrdBC), in which glucose metabolism was directed to pyruvate formate lyase (PFL), was constructed. The hydrogen yield of wild-type strain of 1.08 mol/mol glucose, was enhanced to 1.82 mol/mol glucose in strain SR15. This figure is greater than 90 % of the theoretical hydrogen yield of facultative anaerobes (2.0 mol/mol glucose). Moreover, the specific hydrogen production rate of strain SR15 (13.4 mmol h⁻¹ g⁻¹ dry cell) was 1.4-fold higher than that of wild-type strain. In addition, the volumetric hydrogen production rate increased using the process where cells behaved as an effective catalyst. At 94.3 g dry cell/l, a productivity of 793 mmol h⁻¹ l⁻¹ (20.2 l h⁻¹ l⁻¹ at 37 °C) was achieved using SR15. The reported productivity substantially surpasses that of conventional biological hydrogen production processes and can be a trigger for practical applications.     

l-Ribulose production by an Escherichia coli harboring l-arabinose isomerase from Bacillus licheniformis

Recombinant Escherichia coli harboring the l-arabinose isomerase (BLAI) from Bacillus licheniformis was used as a biocatalyst to produce l-ribulose in the presence of borate. Effects of substrate concentration, the borate to l-arabinose ratio, pH, and temperature on the conversion of l-arabinose to l-ribulose were investigated. l-Ribulose production was efficient when pH was higher than 9 and temperature was higher than 50 °C. Borate addition to the reaction mixture was essential for high conversion of l-arabinose to l-ribulose as it resulted in an equilibrium shift in favor of the product. Under the optimal conditions determined by response surface methodology, the E. coli harboring BLAI produced 375 g l⁻¹ L-ribulose from 500 g l⁻¹ l-arabinose at a reaction time of 60 min, corresponding to a conversion yield of 75% and productivity of 375 g l⁻¹ h⁻¹. When the resting recombinant E. coli cells were recycled, 85% of the yield was obtained even after seven cycles of reuse. The productivity and final concentration of l-ribulose obtained in the present study were the highest yet reported.     

Microscale process evaluation of recombinant biocatalyst libraries: application to Baeyer–Villiger monooxygenase catalysed lactone synthesis

Microscale processing techniques are rapidly emerging as a cost- effective means for parallel experimentation and hence the evaluation of large libraries of recombinant biocatalysts. In this work, the potential of an automated microscale process is demonstrated in a linked sequence of operations comprising fermentation, enzyme induction and bioconversion using three whole-cell biocatalysts each expressing cyclohexanone monoxygenase (CHMO). The biocatalysts, Escherichia coli TOP 10 [pQR239], E. coli JM107 and Acinetobacter calcoaceticus NCIMB 9871, were first produced in 96-deep square well fermentations at various carbon source concentrations (10 and 20 g L⁻¹ glycerol). Following induction of CHMO activity biomass concentrations of up to 6 g_DCW L⁻¹ were obtained. Cells from each fermentation were subsequently used for the Baeyer–Villiger oxidation of bicyclo[3.2.0]hept-2-en-6-one, cyclohexanone and cyclopentanone. Each bioconversion was performed at two initial substrate concentrations (0.5 and 1.0 g L⁻¹) in order to simultaneously explore both substrate specificity and inhibition. The microscale process sequences yielded quantitative and reproducible data for each biocatalyst on maximum growth rate, biomass yield, initial rate of lactone formation, specific biocatalyst activity and bioconversion yield. E. coli TOP 10 [pQR239] was demonstrated to be an efficient biocatalyst showing substrate specificities and substrate inhibition effects in line with previous studies. Finally, in order to show that the data obtained with E. coli TOP 10 [pQR239] at microwell scale (1,000 μL) could be related to larger scales of operation, the process was performed in a 2-L stirred-tank bioreactor. Using conditions designed to enable microwell kinetic measurements under none oxygen-limited conditions, the fermentation and bioconversion data obtained at the two scales showed good quantitative agreement. This study therefore confirms the potential of automated microscale experimentation for the whole-process evaluation of recombinant biocatalyst libraries and the specification of pilot and process scale operating conditions.     

Efficient biocatalytic production of <Emphasis Type="SmallCaps">d</Emphasis>-4-hydroxyphenylglycine by whole cells of recombinant <Emphasis Type="Italic">Ralstonia pickettii</Emphasis>

The first establishment of a homologous expression system in the host Ralstonia pickettii CGMCC1596 using the compatible broad-host-range plasmid pWB5 is described. When whole cells of the recombinant strain R. pickettii MMYY01 (CGMCC1596/pYY05) were used as the biocatalyst to transform dl-4-hydroxyphenylhydantoin (dl-HPH) to d-4-hydroxyphenylglycine (d-HPG), the conversion rate reached 94 % in first 9 h, at a production rate of 2.8 g L⁻¹ h⁻¹, with the rapid reduction of the intermediate [N-carbamoyl-2-(4-hydroxyphenyl)glycine], compared with 80 % in >50 h at a rate of 0.5 g L⁻¹ h⁻¹ for the CGMCC1596. The stability of the recombinant plasmid pYY05 is sufficient for its application in industrial batch fermentation. An alternative strategy for the conversion of dl-HPH to d-HPG by resting CGMCC1596 cells and heterologous DCase expressed by E. coli is discussed.     

Efficient induction of formate hydrogen lyase of aerobically grown <Emphasis Type="Italic">Escherichia coli</Emphasis> in a three-step biohydrogen production process

A three-step biohydrogen production process characterized by efficient anaerobic induction of the formate hydrogen lyase (FHL) of aerobically grown Escherichia coli was established. Using E. coli strain SR13 (fhlA ⁺⁺, ΔhycA) at a cell density of 8.2 g/l medium in this process, a specific hydrogen productivity (28.0 ± 5.0 mmol h⁻¹ g⁻¹ dry cell) of one order of magnitude lower than we previously reported was realized after 8 h of anaerobic incubation. The reduced productivity was attributed partly to the inhibitory effects of accumulated metabolites on FHL induction. To avoid this inhibition, strain SR14 (SR13 ΔldhA ΔfrdBC) was constructed and used to the effect that specific hydrogen productivity increased 1.3-fold to 37.4 ± 6.9 mmol h⁻¹ g⁻¹. Furthermore, a maximum hydrogen production rate of 144.2 mmol h⁻¹ g⁻¹ was realized when a metabolite excretion system that achieved a dilution rate of 2.0 h⁻¹ was implemented. These results demonstrate that by avoiding anaerobic cultivation altogether, more economical harvesting of hydrogen-producing cells for use in our biohydrogen process was made possible.     

Production of ascorbic acid glucoside by alginate-entrapped mycelia of <Emphasis Type="Italic">Aspergillus niger</Emphasis>

The mycelia of Aspergillus niger, cultivated in a medium containing 45 g l⁻¹ maltose, 66 g l⁻¹ yeast extract, and 5 g l⁻¹ K₂HPO₄ at 30°C and 200 rpm, were used as a biocatalyst in the glucosylation of ascorbic acid. Free mycelia from 3-day-old culture, when used in a 6-h reaction with maltose as the acyl donor, gave 16.07 g l⁻¹ ascorbic acid glucoside corresponding to a volumetric productivity of 2.68 g l⁻¹ h⁻¹ and a conversion of 67%. Mycelia from 3-day-old cultures were entrapped in calcium alginate beads and used as a catalyst in the glucosylation of ascorbic acid. An ascorbic acid-to-maltose molar ratio of 1:9 was found to be optimum, and the conversion reached 75% after 12 h. The concentration of ascorbic acid glucoside produced at this molar ratio was 17.95 g l⁻¹, and the productivity was 1.5 g l⁻¹ h⁻¹. The biocatalyst was repeatedly used in a fixed bed bioreactor for the synthesis of ascorbic acid glucoside and approximately 17 g l⁻¹ of ascorbic acid glucoside corresponding to a volumetric productivity of 1.42 g l⁻¹ h⁻¹ was produced in each use. The conversion was retained at 70% in each use. The entrapped mycelia also exhibited exceptionally high reusability and storage stability. The product was purified to 85% by anion exchange and gel permeation chromatography with a final yield of 75%.     

Comparison of microbial hosts and expression systems for mammalian CYP1A1 catalysis

Mammalian cytochrome P450 enzymes are of special interest as biocatalysts for fine chemical and drug metabolite synthesis. In this study, the potential of different recombinant microorganisms expressing rat and human cyp1a1 genes is evaluated for such applications. The maximum specific activity for 7-ethoxyresorufin O-deethylation and gene expression levels were used as parameters to judge biocatalyst performance. Under comparable conditions, E. coli is shown to be superior over the use of S. cerevisiae and P. putida as hosts for biocatalysis. Of all tested E. coli strains, E. coli DH5α and E. coli JM101 harboring rat CYP1A1 showed the highest activities (0.43 and 0.42 U g_CDW⁻¹, respectively). Detection of active CYP1A1 in cell-free E. coli extracts was found to be difficult and only for E. coli DH5α, expression levels could be determined (41 nmol g_CDW⁻¹). The presented results show that efficient expression of mammalian cyp1a1 genes in recombinant microorganisms is troublesome and host-dependent and that enhancing expression levels is crucial in order to obtain more efficient biocatalysts. Specific activities currently obtained are not sufficient yet for fine chemical production, but are sufficient for preparative-scale drug metabolite synthesis.     

High-level succinic acid production and yield by lactose-induced expression of phosphoenolpyruvate carboxylase in ptsG mutant Escherichia coli

Escherichia coli strains with foreign genes under the isopropyl-β-d-thiogalactopyranoside-inducible promoters such as lac, tac, and trc were engineered and considered as the promising succinic acid-producing bacteria in many reports. The promoters mentioned above could also be induced by lactose, which had not been attempted for succinic acid production before. Here, the efficient utilization of lactose as inducer was demonstrated in cultures of the ptsG, ldhA, and pflB mutant strain DC1515 with ppc overexpression. A fermentative process for succinic acid production at high level by this strain was developed. In flask anaerobic culture, 14.86 g l⁻¹ succinic acid was produced from 15 g l⁻¹ glucose with a yield of 1.51 mol mol⁻¹ glucose. In two-stage culture carried out in a 3-l bioreactor, the overall yield and concentration of succinic acid reached to 1.67 mol mol⁻¹ glucose and 99.7 g l⁻¹, respectively, with a productivity of 1.7 g l⁻¹ h⁻¹ in the anaerobic stage. The efficient utilization of lactose as inducer made recombinant E. coli a more capable strain for succinic acid production at large scale.     

Preliminary characterization of a thermostable DNA polymerase I from a mesophilic Bacillus sphaericus strain C3-41

A thermostable DNA polymerase I from a mesophilic Bacillus sphaericus strain C3-41 was characterized in this study. The polI was cloned, sequenced and over-expressed in Escherichia coli. The expressed 110 kDa fusion protein of PolI was stable at 70°C for 1 h. Compared with DNA polymerase I of E. coli (TaKaRa), the relative polymerase activity of this PolI was 3.33 ± 0.1 RFU μl⁻¹ at 37°C using fluorescent quantitative analysis. It showed higher polymerase activity than E. coli PolI at higher temperature, with a relative activity of 3.75 ± 0.1 RFU μl⁻¹ at 70°C. The polI sequence analysis and the protein structure prediction indicated that this protein had a high similarly to other PolI from thermophilic micro-organisms. This information is of importance for future study for evolution of the house-keeping gene polI in entomopathogenic bacterium B. sphaericus.     

Improvement of the multiple-stress tolerance of an ethanologenic <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> strain by freeze-thaw treatment

An effective, simple, and convenient method to improve yeast’s multiple-stress tolerance, and ethanol production was developed. After an ethanologenic Saccharomyces cerevisiae strain SC521 was treated by nine cycles of freeze-thaw, a mutant FT9-11 strain with higher multiple-stress tolerance was isolated, whose viabilities under acetic acid, ethanol, freeze-thaw, H₂O₂, and heat-shock stresses were, respectively, 23-, 26-, 10- and 7-fold more than the parent strain at an initial value 2 × 10⁷ c.f.u. per ml. Ethanol production of FT9-11 was similar (91.5 g ethanol l⁻¹) to SC521 at 30°C with 200 g glucose l⁻¹, and was better than the parent strain at 37°C (72.5 g ethanol l⁻¹), with 300 (111 g ethanol l⁻¹) or with 400 (85 g ethanol l⁻¹) g glucose l⁻¹.     

Alcoholic fermentation of xylose and mixed sugars using recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> engineered for xylose utilization

Previously, a Saccharomyces cerevisiae strain was engineered for xylose assimilation by the constitutive overexpression of the Orpinomyces xylose isomerase, the S. cerevisiae xylulokinase, and the Pichia stipitis SUT1 sugar transporter genes. The recombinant strain exhibited growth on xylose, under aerobic conditions, with a specific growth rate of 0.025 h⁻¹, while ethanol production from xylose was achieved anaerobically. In the present study, the developed recombinant yeast was adapted for enhanced growth on xylose by serial transfer in xylose-containing minimal medium under aerobic conditions. After repeated batch cultivations, a strain was isolated which grew with a specific growth rate of 0.133 h⁻¹. The adapted strain could ferment 20 g l⁻¹ of xylose to ethanol with a yield of 0.37 g g⁻¹ and production rate of 0.026 g l⁻¹ h⁻¹. Raising the fermentation temperature from 30°C to 35°C resulted in a substantial increase in the ethanol yield (0.43 g g⁻¹) and production rate (0.07 g l⁻¹ h⁻¹) as well as a significant reduction in the xylitol yield. By the addition of a sugar complexing agent, such as sodium tetraborate, significant improvement in ethanol production and reduction in xylitol accumulation was achieved. Furthermore, ethanol production from xylose and a mixture of glucose and xylose was also demonstrated in complex medium containing yeast extract, peptone, and borate with a considerably high yield of 0.48 g g⁻¹.     

Temperature management strategy for efficient gene expression in a thermally inducible <Emphasis Type="Italic">Escherichia coli</Emphasis>/bacteriophage system

In a two-phase operation, E. coli containing λSNNU1 (Q ⁻ S ⁻) in the chromosome is typically cultured at 33°C and cloned gene expression is induced by elevating the temperature. At least 40°C is necessary for complete induction of cloned gene expression; however, temperatures above 40°C have been shown to inhibit cloned gene expression. This suggests that a three-phase operation, which has an induction phase between the growth and production phases, may result in higher gene expression. In this study, optimal temperature management strategies were investigated for the three-phase operation of cloned gene expression in thermally inducible E. coli/bacteriophage systems. The optimal temperature for the induction phase was determined to be 40°C. When the temperature of the production stage was 33°C, the optimal time period for the induction phase at 40°C was determined to be 60 min. In contrast, when the temperature of the production phase was 37°C, the optimal period for the induction phase at 40°C was 20∼30 min. When the three-phase temperature and temporal profile were set at a growth phase of 33°C, an induction phase at 40°C for 30 min, and a production phase at 37°C, the highest level of cloned gene expression was achieved.     

Ethanol and xylitol production from glucose and xylose at high temperature by <Emphasis Type="Italic">Kluyveromyces</Emphasis> sp. IIPE453

A yeast strain Kluyveromyces sp. IIPE453 (MTCC 5314), isolated from soil samples collected from dumping sites of crushed sugarcane bagasse in Sugar Mill, showed growth and fermentation efficiency at high temperatures ranging from 45°C to 50°C. The yeast strain was able to use a wide range of substrates, such as glucose, xylose, mannose, galactose, arabinose, sucrose, and cellobiose, either for growth or fermentation to ethanol. The strain also showed xylitol production from xylose. In batch fermentation, the strain showed maximum ethanol concentration of 82 ± 0.5 g l⁻¹ (10.4% v/v) on initial glucose concentration of 200 g l⁻¹, and ethanol concentration of 1.75 ± 0.05 g l⁻¹ as well as xylitol concentration of 11.5 ± 0.4 g l⁻¹ on initial xylose concentration of 20 g l⁻¹ at 50°C. The strain was capable of simultaneously using glucose and xylose in a mixture of glucose concentration of 75 g l⁻¹ and xylose concentration of 25 g l⁻¹, achieving maximum ethanol concentration of 38 ± 0.5 g l⁻¹ and xylitol concentration of 14.5 ± 0.2 g l⁻¹ in batch fermentation. High stability of the strain was observed in a continuous fermentation by feeding the mixture of glucose concentration of 75 g l⁻¹ and xylose concentration of 25 g l⁻¹ by recycling the cells, achieving maximum ethanol concentration of 30.8 ± 6.2 g l⁻¹ and xylitol concentration of 7.35 ± 3.3 g l⁻¹ with ethanol productivity of 3.1 ± 0.6 g l⁻¹ h⁻¹ and xylitol productivity of 0.75 ± 0.35 g l⁻¹ h⁻¹, respectively.     

Improvement of P450(BM-3) whole-cell biocatalysis by integrating heterologous cofactor regeneration combining glucose facilitator and dehydrogenase in E. coli

Escherichia coli BL21, expressing a quintuple mutant of P450_BM-3, oxyfunctionalizes α-pinene in an NADPH-dependent reaction to α-pinene oxide, verbenol, and myrtenol. We optimized the whole-cell biocatalyst by integrating a recombinant intracellular NADPH regeneration system through co-expression of a glucose facilitator from Zymomonas mobilis for uptake of unphosphorylated glucose and a NADP⁺-dependent glucose dehydrogenase from Bacillus megaterium that oxidizes glucose to gluconolactone. The engineered strain showed a nine times higher initial α-pinene oxide formation rate corresponding to a sixfold higher yield of 20 mg g⁻¹ cell dry weight after 1.5 h. The initial total product formation rate was 1,000 μmol h⁻¹ μmol⁻¹ P450 leading to a total of 32 mg oxidized products per gram cell of dry weight after 1.5 h. The physiological functioning of the heterologous cofactor regeneration system was illustrated by a sevenfold increased α-pinene oxide yield in the presence of glucose compared to glucose-free conditions.     

Biotechnological production of <Emphasis Type="SmallCaps">l</Emphasis>-ribose from <Emphasis Type="SmallCaps">l</Emphasis>-arabinose

l-Ribose is a rare and expensive sugar that can be used as a precursor for the production of l-nucleoside analogues, which are used as antiviral drugs. In this work, we describe a novel way of producing l-ribose from the readily available raw material l-arabinose. This was achieved by introducing l-ribose isomerase activity into l-ribulokinase-deficient Escherichia coli UP1110 and Lactobacillus plantarum BPT197 strains. The process for l-ribose production by resting cells was investigated. The initial l-ribose production rates at 39°C and pH 8 were 0.46 ± 0.01 g g⁻¹ h⁻¹ (1.84 ± 0.03 g l⁻¹ h⁻¹) and 0.27 ± 0.01 g g⁻¹ h⁻¹ (1.91 ± 0.1 g l⁻¹ h⁻¹) for E. coli and for L. plantarum, respectively. Conversions were around 20% at their highest in the experiments. Also partially purified protein precipitates having both l-arabinose isomerase and l-ribose isomerase activity were successfully used for converting l-arabinose to l-ribose.     

Factors affecting the production of <Emphasis Type="SmallCaps">l</Emphasis>-xylulose by resting cells of recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

Factors affecting the production of the rare sugar l-xylulose from xylitol using resting cells were investigated. An E. coli BPT228 strain that recombinantly expresses a gene for xylitol dehydrogenase was used in the experiments. The ratio of xylitol to l-xylulose was three times lower in the cytoplasm than in the medium. The effects of pH, temperature, shaking speed, and initial xylitol concentration on l-xylulose production were investigated in shaking flasks using statistical experimental design methods. The highest production rates were found at high shaking speed and at high temperature (over 44°C). The optimal pH for both productivity and conversion was between 7.5 and 8.0, and the optimal xylitol concentration was in the range 250–350 g l⁻¹. A specific productivity of 1.09 ± 0.10 g g⁻¹ h⁻¹ was achieved in a bioreactor. The response surface model based on the data from the shake flask experiments predicted the operation of the process in a bioreactor with reasonable accuracy.     

Characterization of a cold-tolerant plant growth-promoting bacterium Pantoea dispersa 1A isolated from a sub-alpine soil in the North Western Indian Himalayas

Pantoea dispersa strain 1A is a Gram-negative rod-shaped, yellow-pigmented bacterium isolated on nutrient agar plates incubated at 4°C. The identity of the bacterium was confirmed by sequencing of the 16 S rRNA gene. It was capable of growing at temperatures ranging from 4 to 42°C, but maximum growth was observed at 30°C. It is endowed with multiple plant growth promotion attributes such as phosphate solubilization, IAA production, siderophore production and HCN production, which are expressed differentially at sub-optimal temperatures (15 and 4°C). It was able to solubilize phosphate (17.6 μg of P₂O₅ ml⁻¹ day⁻¹), and produce IAA (3.7 μg ml⁻¹ day⁻¹), at 15°C. Qualitative detection of siderophore production and HCN were also observed at 15°C. At 4°C it was found to express all the plant growth promotion attributes. This bacterial isolate was able to positively influence and promote the growth and nutrient uptake parameters of wheat (cv. VL.802) under glasshouse conditions. Hence in the context, of cold wheat-growing environments, it is proposed that Pantoea dispersa 1A (MTCC 8706), could be deployed as an inoculant to attain the desired results of bacterization.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-phenylalanine from glycerol by a recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

The production of l-phenylalanine is conventionally carried out by fermentations that use glucose or sucrose as the carbon source. This work reports on the use of glycerol as an inexpensive and abundant sole carbon source for producing l-phenylalanine using the genetically modified bacterium Escherichia coli BL21(DE3). Fermentations were carried out at 37°C, pH 7.4, using a defined medium in a stirred tank bioreactor at various intensities of impeller agitation speeds (300–500 rpm corresponding to 0.97–1.62 m s⁻¹ impeller tip speed) and aeration rates (2–8 L min⁻¹, or 1–4 vvm). This highly aerobic fermentation required a good supply of oxygen, but intense agitation (impeller tip speed ~1.62 m s⁻¹) reduced the biomass and l-phenylalanine productivity, possibly because of shear sensitivity of the recombinant bacterium. Production of l-phenylalanine was apparently strongly associated with growth. Under the best operating conditions (1.30 m s⁻¹ impeller tip speed, 4 vvm aeration rate), the yield of l-phenylalanine on glycerol was 0.58 g g⁻¹, or more than twice the best yield attainable on sucrose (0.25 g g⁻¹). In the best case, the peak concentration of l-phenylalanine was 5.6 g L⁻¹, or comparable to values attained in batch fermentations that use glucose or sucrose. The use of glycerol for the commercial production of l-phenylalanine with E. coli BL21(DE3) has the potential to substantially reduce the cost of production compared to sucrose- and glucose-based fermentations.     

Continuous ethanol production from wheat straw hydrolysate by recombinant ethanologenic <Emphasis Type="BoldItalic">Escherichia coli</Emphasis> strain FBR5

Continuous production of ethanol from alkaline peroxide pretreated and enzymatically saccharified wheat straw hydrolysate by ethanologenic recombinant Escherichia coli strain FBR5 was investigated under various conditions at controlled pH 6.5 and 35°C. The strain FBR5 was chosen because of its ability to ferment both hexose and pentose sugars under semi-anaerobic conditions without using antibiotics. The average ethanol produced from the available sugars (21.9–47.8 g/L) ranged from 8.8 to 17.3 g/L (0.28–0.45 g/g available sugars, 0.31–0.48 g/g sugar consumed) with ethanol productivity of 0.27–0.78 g l⁻¹ h⁻¹ in a set of 14 continuous culture (CC) runs (16–105 days). During these CC runs, no loss of ethanol productivity was observed. This is the first report on the continuous production of ethanol by the recombinant bacterium from a lignocellulosic hydrolysate.     

Alginate immobilization of recombinant Escherichia coli whole cells harboring l-arabinose isomerase for l-ribulose production

Recombinant Escherichia coli whole cells harboring Bacillus licheniformis l-arabinose isomerase (BLAI) were immobilized with alginate. The operational conditions for immobilization were optimized with response surface methodology. Optimal alginate concentration, Ca²⁺ concentration, and cell mass loading were 1.8% (w/v), 0.1 M, and 44.5 g L⁻¹, respectively. The interactions between Ca²⁺ concentration, alginate concentration, and initial cell mass were significant. After immobilization of BLAI, cross-linking with 0.1% glutaraldehyde significantly reduced cell leakage. The half-life of immobilized whole cells was 150 days, which was 50-fold longer than that of free cells. In seven repeated batches for l-ribulose production, the productivity was as high as 56.7 g L⁻¹ h⁻¹ at 400 g L⁻¹ substrate concentration. The immobilized cells retained 89% of the initial yield after 33 days of reaction. Immobilization of whole cells harboring BLAI, therefore, makes a suitable biocatalyst for the production of l-ribulose, particularly because of its high stability and low cost.