A novel cell modification method used in biotransformation of glycerol to 3-HPA by Lactobacillus reuteri

The aim of the present study was to develop a new cell modification method to facilitate the cell separation from broth. In order to reduce the transfer limitation of substrate and product caused by general immobilization methods in the following biotransformation of glycerol, the carboxyl-functioned superparamagnetic nanoparticle (MNP) was directly attached to the surface of Lactobacillus reuteri for 3-hydroxypropionealdehyde producing. The modification process could be finished in several minutes by just adding MNP fluid into the bulk fermentation broth. The modified cells could be rapidly separated from the solution with the aid of magnetic field. The interaction between cell and MNP was shown by electron microscopy. The efficiency of the cells attached by MNPs for transformation of various concentrations of glycerol (100–400 mM) was studied at various temperatures (25–40 °C) and pH levels (5.8–7.5) with different cell concentrations (7.5–30 g/L). The 3- hydroxypropionealdehyde (HPA)/glycerol molar conversion under optimal condition (30 °C and pH 7) reached 70 %. The inactive modified cell could be reactivated easily by fresh medium and recovered the ability of glycerol conversion. MNPS distributing on cell surface had little adverse effect on cell activity. The modification method simplified the two-step production of 3-HPA by resting L. reuteri. The method of MNPs attached to cell surface is totally different from the traditional immobilization method in which the cell is attached to or entrapped in big carrier. The results obtained in this study showed that carboxyl-functioned MNP could be directly used as cell modification particle and realized cell recycle with the aid of magnetic field in bioprocess.     

Isolation and identification of new lactobacilli from goatling stomach and investigation of reuterin production in Lactobacillus reuteri strains

Five new strains of lactobacilli isolated from goatling??s stomach were identified by molecular?Cbiological approaches. Profiles of fermentable saccharides, Gram staining, and cell morphology were also determined. They were identified as Lactobacillus reuteri (strains KO4b, KO4m, KO5) and as Lactobacillus plantarum (strains KG1z, KG4). In DNA samples of all newly isolated L. reuteri strains as well as in L. reuteri E (Lreu E; originated from lamb), the part of gldC gene, coding large subunit of glycerol dehydratase, that is necessary for 3-hydroxypropionaldehyde (3-HPA; reuterin) production, was amplified using two designed primer sets. However, the 3-HPA production was revealed only in the strain Lreu E. It produced five- or ten-fold lower amount of 3-HPA in comparison with probiotic L. reuteri ATCC 55730 in aerobic or anaerobic conditions, respectively. Moreover, Lreu E completely lost its production ability after ca. five passages in MRS medium. The co-incubation of Lreu E, but not other L. reuteri isolates, with Escherichia coli re-induced 3-HPA production. In the case of L. reuteri ATCC 55730, the 3-HPA production increased more than four times after co-incubation with E. coli.     

Characterization of 1,3-propanediol oxidoreductase (DhaT) from <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> J2B

1,3-propanediol oxidoreductase (DhaT) of Klebsiella pneumoniae converts 3-hydroxypropionaldehyde (3-HPA) to 1,3-propanediol (1,3-PD) during microbial production of 1,3-PD from glycerol. In this study, DhaT from newly isolated K. pneumoniae J2B was cloned, expressed, purified, and studied for its kinetic properties. It showed, on its physiological substrate 3-HPA, higher activity than similar aldehydes such as acetaldehyde, propionaldehyde and butyraldehyde. The turnover numbers (k _cat , 1/s) were estimated as 59.4 for the forward reaction (3-HPA to 1,3-PD at pH 7.0) and 10.0 for the reverse reaction (1,3-PD to 3-HPA at pH 9.0). The Michaelis constants (K _m , mM) were 0.77 (for 3-HPA) and 0.03 (for NADH) for the forward reaction (at pH 7.0), and 7.44 (for 1,3-PD) and 0.23 (for NAD⁺) for the reverse reaction (at pH 9.0). Between these forward and reverse reactions, the optimum temperature and pH were significantly different (37°C and 7.0 vs. 55°C and 9.0, respectively). These results indicate that, under physiological conditions, DhaT mostly catalyzes the forward reaction. The enzyme was seriously inhibited by heavy metal ions such as Ag⁺ and Hg²⁺. DhaT was highly unstable when incubated with its own substrate 3-HPA, indicating the necessity of enhancing its stability for improved 1,3-PD production from glycerol.     

3-Hydroxypropionaldehyde: applications and perspectives of biotechnological production

3-Hydroxypropionaldehyde (3-HPA) forms, together with HPA-hydrate and HPA-dimer, a dynamic, multi-component system (HPA system) used in food preservation, as a precursor for many modern chemicals such as acrolein, acrylic acid, and 1,3-propanediol (1,3-PDO), and for polymer production. 3-HPA can be obtained both through traditional chemistry and bacterial fermentation. To date, 3-HPA has been produced from petrochemical resources as an intermediate in 1,3-PDO production. In vivo, glycerol is converted in one enzymatic step into 3-HPA. The 3-HPA-producing Lactobacillus reuteri is used as a probiotic in the health care of humans and animals. The biotechnological production of 3-HPA from renewable resources is desirable both for use of 3-HPA in foods and for the production of bulk chemicals. The main challenge will be the efficient production and recovery of pure 3-HPA.     

3-Hydroxypropionaldehyde production from crude glycerol by <Emphasis Type="Italic">Lactobacillus diolivorans</Emphasis> with enhanced glycerol uptake

Background

In their quest for sustainable development and effective management of greenhouse gas emissions, our societies pursue a shift away from fossil-based resources towards renewable resources. With 95% of our current transportation energy being petroleum based, the application of alternative, carbon-neutral products—among them biodiesel—is inevitable. In order to enhance the cost structure of biodiesel biorefineries, the valorization of the crude glycerol waste stream into high-value platform chemicals is of major importance.

Results

The purpose of this study is the production of 3-hydroxypropionaldehyde (3-HPA) from biodiesel-derived crude glycerol by Lactobacillus diolivorans. Particular focus is given on overcoming potential limitations of glycerol transport into the cell, in order to use the cells’ total glycerol dehydratase capability towards the formation of 3-HPA as the main product. Recombinant overexpression of the endogenous glycerol uptake facilitating protein PduF results in a significant increase of glycerol conversion by a factor of 1.3. Concomitantly, glycerol dehydratase activity increased from initially 1.70 ± 0.03 U/mg protein to 2.23 ± 0.11 U/mg protein. With this approach, an average productivity of 4.8 g_3-HPA/(g_CDM h) yielding up to 35.9 g/L 3-HPA and 0.91 mol_3-HPA/mol_Glycerol have been obtained.

Conclusion

Lactobacillus diolivorans proves to be a valuable cell factory for the utilization of crude glycerol delivering high-value C3 chemicals like 3-HPA, 1,3-propanediol (1,3-PDO) and 3-hydroxypropionic acid (3-HP). Enhancing the glycerol influx into the cell by genetic engineering was successful paving the way towards the commercial production of 3-HPA.

     

Characterization of a Reuterin-Producing Lactobacillus reuteri BPL-36 Strain Isolated from Human Infant Fecal Sample

A reuterin (3-hydroxypropinaldehyde, 3-HPA)-producing isolate from a human infant fecal sample was identified as Lactobacillus reuteri BPL-36 strain. The organism displayed a broad-spectrum antimicrobial activity. The gene (gdh) encoding a glycerol dehydratase subunit was detected by PCR, thus confirming its reuterin-producing ability. Reuterin concentration of 89.63?mM/mL was obtained in the MRS?Cglycerol medium after 16?h of incubation at 37?°C. The reuterin concentration required to inhibit the growth of Pseudomonas aeruginosa, Escherichia coli O157: H7, Salmonella typhi, Staphylococcus aureus, and Listeria monocytogenes was found to be 1.0, 2.0, 2.0, 4.0, and 10.0?AU/mL, respectively. Antimicrobial efficiency test using BPL-36 cell-free supernatant co-incubated along with different test pathogens was done. Viability of all the tested pathogens decreased with increasing contact time with the cell-free supernatant. S. typhi was observed to be the most susceptible among the tested organisms, and the number of viable cells hugely declined as the contact with cell-free supernatant continued, resulting in a reduction of 6 log cycles (100?% inhibition) of the cells after 4?h of treatment. Production of biogenic amines and degradation of mucin by the reuterin-producing BPL-36 strain were not detected.     

Optimizing aerobic conversion of glycerol to 3-hydroxypropionaldehyde

When cells of Klebsiella pneumoniae NRRL B-199 (ATCC 8724) were grown aerobically on a rich glycerol medium and then suspended in buffer supplemented with semicarbazide and glycerol, aerobic conversion of glycerol to 3-hydroxypropionaldehyde (3-HPA) ensued. Depending on conditions, 0.38 to 0.67 g of 3-HPA were formed per gram of glycerol consumed. This means that up to 83.8% of the carbon invested as glycerol could potentially be recovered as the target product, 3-HPA. Production of 3-HPA was sensitive to the age of cells harvested for resuspension and was nonexistent if cells were cultivated on glucose instead of glycerol as the sole carbon source. Compared with 24- and 72-h cells, 48-h cells produced 3-HPA at the highest rate and with the greatest yield. The cell biomass concentration present during the fermentation was never particularly critical to the 3-HPA yield, but initial fermentation rates and 3-HPA accumulation displayed a linear dependence on biomass concentration that faded when biomass exceeded 3 g/liter. Fermentation performance was a function of temperature, and an optimum initial specific 3-HPA productivity occurred at 32 degrees C, although the overall 3-HPA yield increased continuously within the 25 to 37 degrees C range studied. The pH optimum based on fermentation rate was different from that based on overall yield; 8 versus 7, respectively. Initial glycerol concentrations in the 20 to 50 g/liter range optimized initial 3-HPA productivity and yield.     

Optimizing aerobic conversion of glycerol to 3-hydroxypropionaldehyde.

When cells of Klebsiella pneumoniae NRRL B-199 (ATCC 8724) were grown aerobically on a rich glycerol medium and then suspended in buffer supplemented with semicarbazide and glycerol, aerobic conversion of glycerol to 3-hydroxypropionaldehyde (3-HPA) ensued. Depending on conditions, 0.38 to 0.67 g of 3-HPA were formed per gram of glycerol consumed. This means that up to 83.8% of the carbon invested as glycerol could potentially be recovered as the target product, 3-HPA. Production of 3-HPA was sensitive to the age of cells harvested for resuspension and was nonexistent if cells were cultivated on glucose instead of glycerol as the sole carbon source. Compared with 24- and 72-h cells, 48-h cells produced 3-HPA at the highest rate and with the greatest yield. The cell biomass concentration present during the fermentation was never particularly critical to the 3-HPA yield, but initial fermentation rates and 3-HPA accumulation displayed a linear dependence on biomass concentration that faded when biomass exceeded 3 g/liter. Fermentation performance was a function of temperature, and an optimum initial specific 3-HPA productivity occurred at 32 degrees C, although the overall 3-HPA yield increased continuously within the 25 to 37 degrees C range studied. The pH optimum based on fermentation rate was different from that based on overall yield; 8 versus 7, respectively. Initial glycerol concentrations in the 20 to 50 g/liter range optimized initial 3-HPA productivity and yield.     

Molecular mechanisms of the disturbance caused by malondialdehyde on probiotic Lactobacillus reuteri PL503

This study aimed to provide insight into the molecular and genetic mechanisms implicated in the responses of Lactobacillus reuteri against the oxidative stress induced by malondialdehyde (MDA) by analysing protein oxidation and assessing the uspA and the dhaT genes. Four experimental groups were evaluated depending on the concentration of MDA added in Man, Rogosa and Sharpe (MRS) broth: Control (L. reuteri), 5 µM (L. reuteri + 5 µM MDA), 25 µM (L. reuteri + 25 µM MDA) and 100 µM (L. reuteri + 100 µM MDA). Three replicates were incubated at 37 °C for 24 h in microaerophilic conditions and sampled at 12, 16, 20 and 24 h. The upregulation of the uspA gene by L. reuteri indicates the recognition of MDA as a potential DNA-damaging agent. The dhaT gene, encoding a NADH-dependent-oxidoreductase, was also upregulated at the highest MDA concentrations. This gene was proposed to play a role in the antioxidant response of L. reuteri. The incubation of L. reuteri with MDA increased the production of ROS and caused thiol depletion and protein carbonylation. L. reuteri is proposed to detoxify pro-oxidative species while the underlying mechanism requires further elucidation.     

Cryopreservation of heart cells from the eastern oyster

Summary Conditions were developed to cryopreserve cells from pronase-dissociated atria and ventricles of eastern oysters (Crassostrea virginica). The effect of three concentrations (5, 10, 15%) of the cryoprotectants (dimethyl sulfoxide, glycerol, and propylene glycol), three thawing temperatures (25, 45, 75°C), and three cooling rates (slow, medium, fast) were compared. Cells were frozen at −80°C and plunged in liquid nitrogen. Thawed cells were seeded in 96-well plates and primary cultures were evaluated after 3 d by measuring the metabolic activity using a tetrazolium compound, 3-(4,5-dimethylthiazol-2-yl)-5-( 3-carboxymethoxyphenyl)-2-(4-sulfophenyl)-2H-tetrazolium, and by comparing the relative spreading of cells between treatments. The best conditions for freezing and thawing of cells for each cryoprotectant were selected and a final study was performed to compare cryoprotectants. For this final study, we measured the number of cells and their viability 3 d after thawing, in addition to determining cell metabolic activity and cell spreading. Primary cultures of cells frozen without cryoprotectant and of nonfrozen cells were used as controls in all studies. Atrial cells were best cryopreserved with glycerol at a concentration of 10%, a medium cooling rate, and thawing at 45°C. After thawing, atrial cells showed 53±5% of the metabolic activity, 84±5% of the number, and 92±2% of the viability of nonfrozen cells. For ventricular cells, 10% glycerol, a medium cooling rate, and thawing at 25°C yielded the best results. The thawed ventricular cells showed 83±5% of the metabolic activity, 91±5% of the number, and 96±2% of the viability of nonfrozen cells.     

A Novel NAD<Superscript>+</Superscript>-dependent aldehyde dehydrogenase encoded by the <Emphasis Type="Italic">puuC</Emphasis> gene of <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> DSM 2026 that utilizes 3-hydroxypropionaldehyde as a substrate

3-Hydroxypropionic acid (3-HP), a versatile and valuable platform chemical, has diverse industrial applications; but its biological production from glycerol is often limited by the capability of the enzyme aldehyde dehydrogenase (ALDH) to convert an intermediary compound, 3-hydroxypropionaldehyde (3-HPA), to 3-HP. In this study, we report a new ALDH, PuuC, from Klebsiella pneumoniae DSM 2026, that efficiently converts 3-HPA to 3-HP. The identified gene puuC was cloned, expressed in Escherichia coli, purified, and characterized for its properties. The recombinant enzyme with a molecular weight of 53.8 kDa exhibited broad substrate specificity for various aliphatic aldehydes, especially C₂–C₅ aldehydes. NAD⁺ was the preferred coenzyme for the oxidation of most aliphatic and aromatic aldehydes tested. The optimum pH and temperature for PuuC activity were pH 8.0 and 45°C. The K _m values for 3-HPA and NAD⁺ were 0.48 and 0.09 mM, respectively. The activity of PuuC was enhanced in the presence of reducing agents such as 2-mercaptoethanol or dithiothreitol, while several metal ions, particularly Hg²⁺, Ag⁺, and Cu²⁺ inhibited its activity. The predicted structure of PuuC indicated the presence of K191 and E194 in close proximity to the glycine motif, suggesting that PuuC belongs to class 2 ALDHs.     

Production and regulation of extracellular chitinase from the entomopathogenic fungus Isaria fumosorosea

Extracellular chitinase production by the entomopathogenic fungus, Isaria fumosorosea IF28.2 was studied by using submerged fermentation. Maximum chitinase production (178.34±3.91 mU/mL) was obtained when fermentation was carried out at 25°C for 120 h using 72-h-old mycelium in a medium. The effect of inoculum size on chitinase activity was also observed and maximum chitinase activity (159.41±2.91 mU/mL) was obtained with an inoculum size of 3 discs while an incubation period of 96 h proved the most active inducer of chitinase production yielding a chitinase activity of 186.14±3.81 mU/mL. Colloidal chitin (1.5%, w/v) proved to be the best concentration. The optimum pH for chitinase production was 5.7 while 25°C proved to be the best temperature for chitinase production. Supplementation of additional carbon source like 1.5% N-acetylglucosamine (GlcNAc) showed further enhancement in chitinase production. The divalent metal salts, CaCl₂, MgCl₂ and ZnSO₄, inhibited chitinase activity at 10 and 100 mM concentration, whereas inhibition of chitinase activity by KCl, FeSO₄ and EDTA was observed only at higher concentrations. The results presented in this study increase the knowledge on chitinase production in I. fumosoroseus opening new avenues for the study of the role of this enzyme in virulence against different insect pests during the infection process.     

Characterization of BflI – A Thermostable,Co++-Requiring Isoschizomer of BsiYI from Anoxybacillus Flavithermus

A thermophile, isolated from geothermal areas in the northern Himalayan region of India, was identified by partial 16S rDNA sequence (GenBank accession # AF482430) analysis as Anoxybacillus flavithermus. The isolate produced BflI (REBASE # 4910), a Type II restriction endonuclease, which recognized the sequence 5′-CCNNNNN/NNGG-3′ and was the isoschizomer of BsiYI. The enzyme was purified to homogeneity by passing through Cibacron Blue F3GA agarose, DEAE-cellulose, heparin-agarose and MonoQ FPLC. The purified enzyme (MW 36 kDa) worked best at 60 °C in Promega's buffer C and preferentially required Co⁺⁺(0.4 mM) as cofactor followed by Mg⁺⁺(10 mM) and Mn⁺⁺(1 mM). The enzyme showed high specific activity and worked in the presence of high concentrations of β-mercaptoethanol (200 mM), Triton-X-100 (25%), urea (30%), formamide (6%) and guanidine (40 mM) and showed no star activity in the presence of 40% glycerol. In the absence of any stabilizing agent, BflI retained t _1/2 for at least 96 h at 37 °C, 6 h at 60 °C and 6 months at 4 °C. N-terminal sequencing showed that its first 10 amino acid residues were DFHEDKTIAR. This revised version was published online in July 2006 with corrections to the Cover Date.     

Evaluation of Reuterin Production in Urogenital Probiotic Lactobacillus reuteri RC-14

Classified as a distinct species in 1980, Lactobacillus reuteri strains have been used in probiotic formulations for intestinal and urogenital applications. In the former, the primary mechanism of action of L. reuteri SD2112 (ATCC 55730) has been purported to be its ability to produce the antibiotic 3-hydroxypropionaldehyde (3-HPA), also known as reuterin. In the vagina, it has been postulated that probiotic Lactobacillus reuteri RC-14 does not require reuterin production but mediates a restoration of the normal microbiota via hydrogen peroxide, biosurfactant, lactic acid production, and immune modulation. The aim of the present study was to determine whether strain RC-14 produced reuterin. Using PCR and DNA dot blot analyses, numerous Lactobacillus species, including RC-14, were screened for the presence of the gene encoding the large subunit of glycerol dehydratase (gldC), the enzyme responsible for reuterin production. In addition, lactobacilli were grown in glycerol-based media and both high-performance liquid chromatography and a colorimetric assay were used to test for the presence of reuterin. L. reuteri RC-14 was determined to be negative for gldC sequences, as well as for the production of reuterin when cultured in the presence of glycerol. These findings support that the probiotic effects of L. reuteri RC-14, repeatedly demonstrated during numerous studies of the intestine and vagina, are independent of reuterin production.     

Investigation of the transport of intact glutathione in human and rat type II pneumocytes

The aim of the study was to investigate whether there is transmembrane transport of intact glutathione ([³H]-GSH, 0.1 μCi) in rat and human type II pneumocytes (T2P), and if this transport might be dependent on the redox state of the extracellular fluid. The T2P were pretreated with acivicin (250 μM) to inhibit γ-glutamyl-transferase activity and with L-buthionine-[SR]-sulfoximine (1 mM) to inhibit intracellular GSH synthesis. After 48 h in culture, initial GSH influx rate was 0.70 ± 0.20 nmol/min/mg protein (37°C) and 0.35 ± 0.04 nmol/min/mg protein (4°C) during the first 5 min in rat T2P. In human T2P, the initial GSH influx rate was 0.36 ± 0.30 nmol/min/mg protein (37°C) and 0.32 ± 0.06 nmol/min/mg protein (4°C) during the first 10 min. Thereafter no further influx was found. The influx of 1 mM GSH in freshly isolated rat and human T2P in suspension was 2.3 ± 0.3 and 1.2 ± 0.3 nmol/mg protein after 15 min at 37°C, and 2.8 ± 0.2 and 1.0 ± 0.3 nmol/mg protein at 4°C, respectively. When GSH influx was studied at different concentrations between 0 and 40 mM, a linear increase without saturation or difference between 37°C and 4°C was found. Preexposure to ouabain had no effect on GSH influx. Efflux of GSH was stimulated and influx inhibited by preexposure of the cells to reduced thiols, while disulphides inhibited efflux and favoured inward uptake. Thus, in human and rat T2P a GSH-carrier exists which operates as an effluxer. At GSH concentrations in the physiological range no uptake is seen, but some uptake can be observed at GSH concentrations above normal physiological levels. The uptake appears to be energy-independent and non-saturable. Efflux of GSH is stimulated and influx inhibited by reduced thiols, while disulphides inhibit the efflux and favour inward uptake. GSH uptake in T2P thus may depend on concentration gradients and driving forces, such as the redox state of the extracellular fluid.     

Shifts in the fermentation balance of Lactobacillus reuteri. In the presence of glycerol

Summary The influence of glycerol (100 mM) on the growth kinetic and the end-products formation by Lactobacillus reuteri growing on maltose (29 mM) was examined in aerobiosis and anaerobiosis. The presence of glycerol in aerated cultures changed the maltose consumption but not the growth rate nor the fermentation balance. In a nitrogen atmosphere, L. reuteri was not able to grow on maltose alone. In the presence of both, maltose and glycerol, L. reuteri changed its fermentation pattern, producing 58 mM 1,3-propanediol as the major end product.     

Alkaline conditions stimulate the production of 1,3-propanediol in Lactobacillus panis PM1 through shifting metabolic pathways

A novel Lactobacillus panis PM1 isolate was found to be capable of converting glycerol to 1,3-propanediol (1,3-PDO), an increasingly valuable commodity chemical. In this study the effects of various process parameters, including glucose and glycerol concentrations, inoculum size, temperature, aeration, pH, and carbon source were examined to determine the optimal conditions for the production of 1,3-PDO using a culture method simulating late log to early stationary phases. Inoculum size did not influence the production of 1,3-PDO, and temperature variance showed similar 1,3-PDO production between 25 and 37 °C under the examined conditions. Glycerol concentration and pH played a primary role in the final concentration of 1,3-PDO. The highest production occurred at 150–250 mM glycerol when 50 mM glucose was available. Alkaline initial conditions (pH 9–10) stimulated the production of 1,3-PDO which concurrently occurred with increased acetic acid production. Under these conditions, 213.6 mM of 1,3-PDO were produced from 300 mM glycerol (conversion efficiency was 71 %). These observations indicated that the production of 1,3-PDO was associated with the shift of the metabolic end-product ethanol to acetic acid, and that this shift resulted in an excess concentration of NADH available for the processing of glycerol to 1,3-PDO.     

Impact of fermentation pH and temperature on freeze-drying survival and membrane lipid composition of <Emphasis Type="Italic">Lactobacillus coryniformis</Emphasis> Si3

During the industrial stabilization process, lactic acid bacteria are subjected to several stressful conditions. Tolerance to dehydration differs among lactic acid bacteria and the determining factors remain largely unknown. Lactobacillus coryniformis Si3 prevents spoilage by mold due to production of acids and specific antifungal compounds. This strain could be added as a biopreservative in feed systems, e.g. silage. We studied the survival of Lb. coryniformis Si3 after freeze-drying in a 10% skim milk and 5% sucrose formulation following different fermentation pH values and temperatures. Initially, a response surface methodology was employed to optimize final cell density and growth rate. At optimal pH and temperature (pH 5.5 and 34 °C), the freeze-drying survival of Lb. coryniformis Si3 was 67% (±6%). The influence of temperature or pH stress in late logarithmic phase was dependent upon the nature of the stress applied. Heat stress (42 °C) did not influence freeze-drying survival, whereas mild cold- (26 °C), base- (pH 6.5), and acid- (pH 4.5) stress significantly reduced survival. Freeze-drying survival rates varied fourfold, with the lowest survival following mild cold stress (26 °C) prior to freeze-drying and the highest survival after optimal growth or after mild heat (42 °C) stress. Levels of different membrane fatty acids were analyzed to determine the adaptive response in this strain. Fatty acids changed with altered fermentation conditions and the degree of membrane lipid saturation decreased when the cells were subjected to stress. This study shows the importance of selecting appropriate fermentation conditions to maximize freeze-drying viability of Lb. coryniformis as well as the effects of various unfavorable conditions during growth on freeze-drying survival.     

Effect of temperature on <Emphasis Type="SmallCaps">d</Emphasis>-arabitol production from lactose by <Emphasis Type="Italic">Kluyveromyces lactis</Emphasis>

d-Arabitol production from lactose by Kluyveromyces lactis NBRC 1903 has been studied by following the time courses of concentrations of cell mass, lactose, d-arabitol, ethanol, and glycerol at different temperatures. It was found that temperature is a key factor in d-arabitol production. Within temperatures ranging from 25 to 39°C, the highest d-arabitol concentration of 99.2 mmol l⁻¹ was obtained from 555 mmol l⁻¹ of lactose after 120 h of batch cultivation at 37°C. The yield of d-arabitol production on cell mass growth increased drastically at temperatures higher than 35°C, and the yield reached 1.07 at 39°C. Increasing the cell mass concentration two-fold after 24 h of culture growth at 37°C, the d-arabitol concentration further increased to 168 mmol l⁻¹. According to the distribution of the metabolic products, metabolic changes related to growth phase were also discussed. The stationary-phase K. lactis cells in the batch culture that is started with exposing the precultured inoculum to high osmotic stress, high oxidative stress, and high heat stress are found to be preferable for d-arabitol production.     

3-Hydroxypropionaldehyde guided glycerol feeding strategy in aerobic 1,3-propanediol production by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

3-Hydroxypropionaldehyde (3-HPA) is a toxic intermediary metabolite in the biological route of 1,3-propanediol biosynthesis from glycerol. 3-HPA accumulated in culture medium would arouse an irreversible cessation of the fermentation process. The role of substrate (glycerol) on 3-HPA accumulation in aerobic fermentation was investigated in this paper. 1,3-Propanediol oxidoreductase and glycerol dehydratase, two key enzyme catalyzing reactions of 3-HPA formation and consumption, were sensitive to high concentration of 3-HPA. When the concentration of 3-HPA increased to a higher level in medium (ac 10 mmol/L), the activity of 1,3-propanediol oxidoreductase in cell decreased correspondingly, which led to decrease of the 3-HPA conversion rate, then the 3-HPA concentration increasing was accelerated furthermore. 3-HPA accumulation in culture medium was triggered by this positive feedback mechanism. In the cell exponential growth phase, the reaction catalyzed by 1,3-propanediol oxidoreductase was the rate limiting step in 1,3-propanediol production. The level of 3-HPA in culture medium could be controlled by the substrate (glycerol) concentration, and lower level of glycerol could avoid 3-HPA accumulating to a high, lethal concentration. In fed batch fermentation, under the condition of initial glycerol concentration 30 g/L, and keeping glycerol concentration lower than 7–8 g/L in cell exponential growth phase, 3-HPA accumulation could not be incurred. Based on this result, a glycerol feeding strategy was set up in fed batch fermentation. Under the optimized condition, 50.1 g/L of 1,3-propanediol was produced in 24 h, and 73.1 g/L of final 1,3-propanediol concentration was obtained in 54 h.