D-Tagatose production in the presence of borate by resting Lactococcus lactis cells harboring Bifidobacterium longum L-arabinose isomerase.

Bifidobacterium longum NRRL B-41409 L-arabinose isomerase (L-AI) was overexpressed in Lactococcus lactis using a phosphate depletion inducible expression system. The resting L. lactis cells harboring the B. longum L-AI were used for production of D-tagatose from D-galactose in the presence of borate buffer. Multivariable analysis suggested that high pH, temperature and borate concentration favoured the conversion of D-galactose to D-tagatose. Almost quantitative conversion (92 %) was achieved at 20 g L⁻¹ substrate and at 37.5 °C after 5 days. The D-tagatose production rate of 185 g L⁻¹ day ⁻¹ was obtained at 300 g L⁻¹ galactose, at 1.15 M borate, and at 41 °C during 10 days when the production medium was changed every 24 h. There was no significant loss in productivity during ten sequential 24 h batches. The initial D-tagatose production rate was 290 g L⁻¹ day⁻¹ under these conditions.

Production of L-xylose from L-xylulose using Escherichia coli L-fucose isomerase.

L-Xylulose was used as a raw material for the production of L-xylose with a recombinantly produced Escherichia coli L-fucose isomerase as the catalyst. The enzyme had a very alkaline pH optimum (over 10.5) and displayed Michaelis-Menten kinetics for L-xylulose with a K(m) of 41 mM and a V(max) of 0.23 µmol/(mg min). The half-lives determined for the enzyme at 35 °C and at 45 °C were 6h 50 min and 1h 31 min, respectively. The reaction equilibrium between L-xylulose and L-xylose was 15:85 at 35 °C and thus favored the formation of L-xylose. Contrary to the L-rhamnose isomerase catalyzed reaction described previously [14]L-lyxose was not detected in the reaction mixture with L-fucose isomerase. Although xylitol acted as an inhibitor of the reaction, even at a high ratio of xylitol to L-xylulose the inhibition did not reach 50%.

Effect of glycosylation and additional domains on the thermostability of a family 10 xylanase produced by Thermopolyspora flexuosa.

The effects of different structural features on the thermostability of Thermopolyspora flexuosa xylanase XYN10A were investigated. A C-terminal carbohydrate binding module had only a slight effect, whereas a polyhistidine tag increased the thermostability of XYN10A xylanase. In contrast, glycosylation at Asn26, located in an exposed loop, decreased the thermostability of the xylanase. The presence of a substrate increased stability mainly at low pH.

Factors affecting the production of L-xylulose by resting cells of recombinant Escherichia coli.

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 degrees 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.

A new and efficient phosphate starvation inducible expression system for Lactococcus lactis.

A new expression system for Lactococcus lactis was developed. The system is based on a phosphate starvation inducible pstF promoter of L. lactis MG1363. Intracellular beta-galactosidase and secreted alpha-amylase were produced using this tightly regulated system. No evidence of regulatory sites in regions of the 5'-end of the pstF coding sequence was found. High expression levels of the beta-galactosidase gene were obtained using the original pstF RBS in a phosphate-depleted medium. The results suggested that with the phosphate starvation inducible system, it is possible to achieve expression levels comparable to the ones obtained with the widely used nisin-controlled gene expression system (NICE). A specific beta-galactosidase activity of 670 microkat g(-1) using a phosphate-depleted medium and an alpha-amylase activity of 3.6 microkat l(-1) in a bioreactor cultivation were produced. The advantages of the current expression system include that no prior removal of phosphate from the medium in bioreactor scale is required, and no additions of inducing agents are needed. Furthermore, the system can be operated in L. lactis without introduction of regulatory genes into the host.

Bioreactor for solid-state cultivation of Phlebiopsis gigantea.

Phlebiopsis gigantea fungus used in biological control of root rot is currently cultivated commercially in disposable, sterilizable plastic bags. A novel packed bed bioreactor was designed for cultivating P. gigantea and compared to the plastic bag method and to a tray bioreactor. The spore viability of 5.4 x 10(6) c.f.u./g obtained with the packed bed bioreactor was of the same order of magnitude as the viabilities obtained with the other cultivation methods. Furthermore, the packed bed bioreactor was less time and space consuming and easier to operate than the tray bioreactor.

Bioscience, bioinnovations, and bioethics.

Biosciences and their applications, which we call biotechnology, have affected human society in many ways. Great hopes have been set on future biotechnology. The future depends on three key issues. First, we need good science. Recent developments in biosciences have surprised us in many ways. I shall explain in this article how. Secondly, we need structured innovation systems in order to commercialize our discoveries. Europe is slow in this respect compared to our Japanese and American competitors and may lose in the competition. I shall describe the Finnish innovation chain using the rewarded Otaniemi model as an example of how commercialization can be done in a systematic way. Thirdly, we need norms to guide what to do and where to go. Bioethics is probably the most neglected of the three key issues. With modern biotechnology we are able to do things that should worry every citizen, but the ethical discussion has been largely neglected or the discussion in our pluralistic society is leading nowhere. I shall finally discuss these problems from a historical perspective.

Protein engineering: opportunities and challenges.

The extraordinary properties of natural proteins demonstrate that life-like protein engineering is both achievable and valuable. Rapid progress and impressive results have been made towards this goal using rational design and random techniques or a combination of both. However, we still do not have a general theory on how to specify a structure that is suited to a target function nor can we specify a sequence that folds to a target structure. There is also overreliance on the Darwinian blind search to obtain practical results. In the long run, random methods cannot replace insight in constructing life-like proteins. For the near future, however, in enzyme development, we need to rely on a combination of both.

A rare sugar xylitol. Part I: the biochemistry and biosynthesis of xylitol.

The rare sugar xylitol is a five-carbon polyol (pentitol) that has beneficial health effects. Xylitol has global markets and, therefore, it represents an alternative to current dominant sweeteners. The research on microbial reduction of D-xylose to xylitol has been focused on metabolically engineered Saccharomycess cerevisiae and Candida strains. The Candida strains have an advantage over the metabolically engineered S. cerevisiae in terms of D-xylose uptake and maintenance of the intracellular redox balance. Due to the current industrial scale production of xylitol, it has become an inexpensive starting material for the production of other rare sugar. The first part of this mini-review concentrates on the biochemistry of xylitol biosynthesis and the problems related to intracellular redox balance.

A rare sugar xylitol. Part II: biotechnological production and future applications of xylitol.

Xylitol is the first rare sugar that has global markets. It has beneficial health properties and represents an alternative to current conventional sweeteners. Industrially, xylitol is produced by chemical hydrogenation of D-xylose into xylitol. The biotechnological method of producing xylitol by metabolically engineered yeasts, Saccharomyces cerevisiae or Candida, has been studied as an alternative to the chemical method. Due to the industrial scale of production, xylitol serves as an inexpensive starting material for the production of other rare sugars. The second part of this mini-review on xylitol will look more closely at the biotechnological production and future applications of the rare sugar, xylitol.

A chemostat study of Streptomyces peucetius var. caesius N47.

The behavior of Streptomyces peucetius var. caesius N47 was studied in a glucose limited chemostat with a complex cultivation medium. The steady-state study yielded the characteristic constants mu (max) over 0.10 h(-1), Y (XS) 0.536 g g(-1), and m(S) 0.54 mg g(-1) h(-1). The product of secondary metabolism, epsilon-rhodomycinone, was produced with characteristics Y (PX) 12.99 mg g(-1) and m (P) 1.20 mg g(-1) h(-1). Significant correlations were found for phosphate and glucose consumption with biomass and epsilon-rhodomycinone production. Metabolic flux analysis was conducted to estimate intracellular fluxes at different dilution rates. TCA, PPP, and shikimate pathway fluxes exhibited bigger values with production than with growth. Environmental perturbation experiments with temperature, airflow, and pH changes on a steady-state chemostat implied that an elevation of pH could be the most effective way to shift the cells from growing to producing, as the pH change induced the biggest transient increase to the calculated epsilon-rhodomycinone flux.

Characterization of genes involved in fructose utilization by Lactobacillus fermentum.

The genes encoding phosphoglucose isomerase (fruI) and fructokinase (fruK) of Lactobacillus fermentum NRRL-B-1932 were sequenced. They constituted an operon, which is involved in fructose metabolism of this strain by channeling intracellular fructose into the phosphoketolase pathway. A third open reading frame, unkR, upstream of the operon was identified as homologous to genes of LacI/GalR family repressors. The UnkR repressor's role in transcriptional control of the fruIK operon could, however, not be established by electrophoretic mobility shift assay (EMSA) analysis. Sequence analysis revealed two putative catabolite responsive elements (cre) in the promoter region of fruIK suggesting that the fruIK operon is under negative regulatory control by carbon catabolite repression. Expression and enzyme activity data were compatible with the assumption that the fruIK operon is repressed by glucose. No sugar specific phosphoenolpyruvate sugar transferase system activity for the transport of fructose, glucose, sucrose or mannose could be detected in L. fermentum NRRL-B-1932 cells, which suggest that fructose is taken up by a permease system.

Modeling and simulation of Streptomyces peucetius var. caesius N47 cultivation and epsilon-rhodomycinone production with kinetic equations and neural networks.

This study focuses on comparing different kinetic growth models and the use of neural networks in the batch cultivation of Streptomyces peucetius var. caesius producing epsilon-rhodomycinone. Contois, Monod and Teissier microbial growth models were used as well as the logistic growth modeling approach, which was found best in the simulations of growth and glucose consumption in the batch growth phase. The lag phase was included in the kinetic model with a CO2 trigger and a delay factor. Substrate consumption and product formation were included as Luedeking-Piret and logistic type equations, respectively. Biomass formation was modeled successfully with a 6-8-2 network, and the network was capable of biomass prediction with an R2-value of 0.983. Epsilon-rhodomycinone production was successfully modeled with a recursive 8-3-1 network capable of epsilon-rhodomycinone prediction with an R2-value of 0.903. The predictive power of the neural networks was superior to the kinetic models, which could not be used in predictive modeling of arbitrary batch cultivations.

Production of recombinant HIV-1 Nef (negative factor) protein using Pichia pastoris and a low-temperature fed-batch strategy.

In the present paper we describe the cloning and extracellular expression of the HIV-1 Nef (negative factor) protein utilizing the yeast Pichia pastoris, as well as the successful use of a low-temperature fed-batch strategy for decreasing end-product degradation by proteases. The nef gene in a pPICZalphaA vector was integrated into the genome of three different P. pastoris strains, namely X-33, GS115 and KM71H. On the basis of its efficient growth and production characteristics the wild-type strain (X-33) was found to be the best choice. The decreased end-product degradation at low temperatures was not due to lower amounts of proteases but due to their diminished activity. The yield of biomass from methanol was improved 1.44-fold utilizing the low-temperature strategy compared with the standard fermentation. Purification of histidine-tagged Nef was performed in one step using a Ni(2+)-nitrilotriacetate-Sepharose column. The purified product was characterized by SDS/PAGE, Western blotting, matrix-assisted laser-desorption ionization-time-of-flight MS, reversed-phase HPLC and N-terminal-sequence analysis.

Production of xylitol from D-xylose by recombinant Lactococcus lactis.

The D-xylose reductase from Pichia stipitis CBS 5773 and the xylose transporter from Lactobacillus brevis ATCC 8287 were expressed in active form in Lactococcus lactis NZ9800. Xylitol production was investigated using non-growing recombinant cells in high cell-density under microaerobic conditions in the presence of xylose and glucose. Besides xylose, the recombinant strain with xylose reductase activity reduced l-arabinose and D-ribose in significant extent to the corresponding pentitols. The ratio of xylitol produced per glucose consumed was almost 10-fold higher under glucose limitation than the ratio in the presence of excess initial glucose. The co-expression of the xylose transporter with the xylose reductase did not increase the efficiency of xylitol production appreciably when compared to the strain in which only the xylose reductase gene was expressed. A fed-batch experiment with high initial xylose concentration (160 gl(-1)) under glucose limitation was carried out using the strain co-expressing xylose reductase and xylose transporter genes. The xylitol yield from xylose was 1.0 mol mol(-1) and the ratio of xylitol produced per glucose consumed was 2.5 mol mol(-1). The volumetric productivity was 2.72 gl(-1)h(-1) at 20 h. Of the xylose initially present, 34% was consumed. Analysis of the fermentation metabolites revealed a shift from homolactic to mixed acid fermentation at early stages of the experiment.

Optimization of a Bifidobacterium longum production process.

Bifidobacteria are used as probiotics mainly in the dairy industry as cell suspensions or as freeze-dried additives. So far there have been no reports on a thorough investigation on factors influencing the production process or a statistical approach to the optimization thereof. A 2(8-4) fractional factorial design was used in determining the critical parameters influencing bioreactor cultivations of Bifidobacterium longum ATCC 15707. Glucose, yeast extract and l-cysteine concentrations were found critical for the cultivation of this strain. Glucose and yeast extract concentrations were further studied together with temperature in a three factor central composite design. The optimized cultivation conditions were temperature 40 degrees C, yeast extract concentration 35 gl(-1) and glucose concentration 20 gl(-1). Freeze-drying of frozen cell suspensions of B. longum was studied first in controlled temperatures and thereafter with temperature programming experiments. The results were statistically evaluated. A temperature program with a 2 h temperature gradient from -10 to 0 degrees C, a 10 h temperature gradient from 0 to +10 degrees C and a 12 h temperature hold at +10 degrees C was found best for the freeze-drying process. Temperature programming reduced drying times by over 50% and improved the product activity by over 160%.

Stochastic boundary molecular dynamics simulation of L-ribose in the active site of Actinoplanes missouriensis xylose isomerase and its Val135Asn mutant with improved reaction rate.

We used molecular dynamics simulations to study how a non-natural substrate, L-ribose, interacts with the active site of Actinoplanes missouriensis xylose isomerase. The simulations showed that L-ribose does not stay liganded in the active site in the same way as D-xylose, in which the oxygens O2 and O4 are liganded to the metal M1. The oxygen O4 of L-ribose moved away from the metal M1 to an upside down position. Furthermore, the distances of the carbons C1 and C2 of L-ribose to the catalytic metal M2 were higher than in the case of D-xylose. These findings explain the extremely low reaction rate of xylose isomerase with L-ribose. The mutation V135N close to the C5-OH of the substrate increased the reaction efficiency 2- to 4-fold with L-ribose. V135N did not affect the reaction with D-xylose and L-arabinose, whereas the reaction with D-glucose was impaired, probably due to a hydrogen bond between Asn-135 and the substrate. When L-ribose was the substrate, Asn-135 formed a hydrogen bond to Glu-181. As a consequence, O4 of L-ribose stayed liganded to the metal M1 in the V135N mutant in molecular dynamics simulations. This explains the decreased K(m) of the V135N mutant with L-ribose.

Improved mannitol production by a random mutant of Leuconostoc pseudomesenteroides.

A mutant of Leuconostoc pseudomesenteroides ATCC12291 that was unable to grow on fructose was constructed by chemical mutagenesis. The fructose uptake of this mutant, designated as BPT143, was unaltered and allowed fructose still to be converted into mannitol when glucose was present in the growth medium. The mutant grew and consumed fructose faster than the parent strain when grown in a medium containing both glucose and fructose. The specific activity of fructokinase, the enzyme involved in phosphorylation of fructose to fructose-6-phosphate, was decreased to about 10% of that of the parent strain, and resulted in a reduced leakage of fructose into the phosphoketolase (PK) pathway. The yield of mannitol from fructose was improved from 74 to 86 mol%. The increased fructose consumption rate and higher mannitol yield of the mutant also resulted in improvement of volumetric mannitol productivity. In addition, isolation and characterization of the wild type L. pseudomesenteroides fructokinase gene (fruK) was performed. DNA sequence analysis of the fruK gene region of BPT143 revealed only one silent mutation which does not explain the highly reduced fructokinase activity of the mutant. The genetic characterization of fruK was completed by analyzing the expression, size and 5' end of fruK transcripts. Expression data with BPT143, revealing absence of fruK transcripts, was in accordance with the reduced fructokinase activity of the mutant.

Structure of the exopolysaccharide produced by Enterobacter amnigenus.

The bacterial species Enterobacter amnigenus was isolated from sugar beets harvested in Finland. It produced an exopolysaccharide rich in l-fucose, which gave viscous water solutions. Its primary structure was determined mainly by NMR spectroscopy and ESIMS of oligosaccharides and a polysaccharide with decreased molecular weight, obtained by Smith degradation of the O-deacetylated native polymer [carbohydrate structure: see text]

Xylanase production by Trichoderma reesei Rut C-30 grown on L-arabinose-rich plant hydrolysates.

The suitability of L-arabinose-rich plant hydrolysates as carbon sources and inducers of xylanase production in Trichoderma reesei Rut C-30 was tested. Significantly higher xylanase activities were obtained in cultures on oat husk and sugar beet pulp hydrolysates than on lactose. In batch culture with oat husk hydrolysate and lactose, the xylanase activity was about 9 times higher ( approximately 510 IU/ml) than in lactose ( approximately 60 IU/ml). Even higher xylanase activity ( approximately 630 IU/ml) was obtained when the batch cultivations were done on sugar beet pulp hydrolysate and lactose. In a fed-batch culture using oat husk hydrolysate-lactose the xylanase activity was as high as 1350 IU/ml in 4 days. The cellulase production clearly decreased when T. reesei was cultured on both hydrolysates compared to the cultivation on lactose. Moreover, the relative amounts of the xylanases I-III were similar regardless the used carbon source.