The effect of thermostabilising mutations on the pressure stability of Trichoderma reesei GH11 xylanase.

We studied the pressure stability of disulphide bridge mutants of Trichoderma reesei XYNII at 500-5000 bar. The inactivation of XYNII and its mutants was strongest above 4000 bar. The pressure stability correlated with the thermostability order of the XYNII mutants, indicating that the stabilising mutations in protein regions important for thermostability also protect the enzyme at high pressure. In combination with high pressure, a mild heating had already inactivated the wild-type enzyme; the thermostabilising mutations largely counteracted this effect. At a low temperature, the mutations did not have any remarkable pressure stabilisation effect. Thus, thermal inactivation appeared to dominate over pressure inactivation at higher temperatures. Kinetic calculations indicated that pressure compressibility correlated with the thermostability of xylanase mutants.

Developing a multipoint titration method with a variable dose implementation for anaerobic digestion monitoring.

Determination of metabolites from an anaerobic digester with an acid base titration is considered as superior method for many reasons. This paper describes a practical at line compatible multipoint titration method. The titration procedure was improved by speed and data quality. A simple and novel control algorithm for estimating a variable titrant dose was derived for this purpose. This non-linear PI-controller like algorithm does not require any preliminary information from sample. Performance of this controller is superior compared to traditional linear PI-controllers. In addition, simplification for presenting polyprotic acids as a sum of multiple monoprotic acids is introduced along with a mathematical error examination. A method for inclusion of the ionic strength effect with stepwise iteration is shown. The titration model is presented with matrix notations enabling simple computation of all concentration estimates. All methods and algorithms are illustrated in the experimental part. A linear correlation better than 0.999 was obtained for both acetate and phosphate used as model compounds with slopes of 0.98 and 1.00 and average standard deviations of 0.6% and 0.8%, respectively. Furthermore, insensitivity of the presented method for overlapping buffer capacity curves was shown.

Biotechnological production of L-ribose from L-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 degrees 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.

Metabolic engineering of Lactobacillus plantarum for production of L-ribulose.

L-Ribulose is a rare and expensive sugar that can be used as a precursor for the production of other rare sugars of high market value such as L-ribose. In this work we describe a production process for L-ribulose using L-arabinose, a common component of polymers of lignocellulosic materials, as the starting material. A ribulokinase-deficient mutant of the heterofermentative lactic acid bacterium Lactobacillus plantarum NCIMB8826 was constructed. Expression of araA, which encodes the critical enzyme L-arabinose isomerase, was repressed by high glucose concentrations in batch cultivations. A fed-batch cultivation strategy was therefore used to maximize L-arabinose isomerase production during growth. Resting cells of the ribulokinase-deficient mutant were used for the production of L-ribulose. The isomerization of L-arabinose to L-ribulose was very unfavorable for L-ribulose formation. However, high L-ribulose yields were obtained by complexing the produced L-ribulose with borate. The process for L-ribulose production in borate buffer by resting cells was optimized using central composite designs. The experiment design suggested that the process has an optimal operation point around an L-arabinose concentration of 100 g liter(-1), a borate concentration of 500 mM, and a temperature of 48 degrees C, where the statistical software predicted an initial L-ribulose production rate of 29.1 g liter(-1) h(-1), a best-achievable process productivity of 14.8 g liter(-1) h(-1), and a conversion of L-arabinose to L-ribulose of 0.70 mol mol(-1).

On-line biomass measurements in bioreactor cultivations: comparison study of two on-line probes.

Two on-line probes for biomass measurement in bioreactor cultivations were evaluated. One probe is based on near infrared (NIR) light absorption and the other on dielectric spectroscopy. The probes were used to monitor biomass production in cultivations of several different microorganisms. Differences in NIR probe response compared to off-line measurement methods revealed that the most significant factor affecting the response was cell shape. The NIR light absorption method is more developed and reliable for on-line in situ biomass estimation than dielectric spectroscopy. The NIR light absorption method is, however, of no significant use, when the cultivation medium is not clear, and especially in processes using adsorbents or solid matrix for the microorganism to grow on. The possibilities offered by dielectric spectroscopy are impressive, but the on-line probe technology needs to be

Cloning and expression of a xylitol-4-dehydrogenase gene from Pantoea ananatis.

The Pantoea ananatis ATCC 43072 mutant strain is capable of growing with xylitol as the sole carbon source. The xylitol-4-dehydrogenase (XDH) catalyzing the oxidation of xylitol to L-xylulose was isolated from the cell extract of this strain. The N-terminal amino acid sequence of the purified protein was determined, and an oligonucleotide deduced from this peptide sequence was used to isolate the xylitol-4-dehydrogenase gene (xdh) from a P. ananatis gene library. Nucleotide sequence analysis revealed an open reading frame of 795 bp, encoding the xylitol-4-dehydrogenase, followed by a 5' region of another open reading frame encoding an unknown protein. Results from a Northern analysis of total RNA isolated from P. ananatis ATCC 43072 suggested that xdh is transcribed as part of a polycistronic mRNA. Reverse transcription-PCR analysis of the transcript confirmed the operon structure and suggested that xdh was the first gene of the operon. Homology searches revealed that the predicted amino acid sequence of the P. ananatis XDH shared significant identity (38 to 51%) with members of the short-chain dehydrogenase/reductase family. The P. ananatis xdh gene was successfully overexpressed in Escherichia coli, XDH was purified to homogeneity, and some of its enzymatic properties were determined. The enzyme had a preference for NAD+ as the cosubstrate, and in contrast to previous reports, the enzyme also showed a side activity for the D-form of xylulose. Xylitol was converted to L-xylulose with a high yield (>80%) by the resting recombinant cells, and the L-xylulose was secreted into the medium. No evidence of D-xylulose being synthesized by the recombinant cells was found.

Optimization of Streptomyces peucetius var. caesius N47 cultivation and epsilon-rhodomycinone production using experimental designs and response surface methods.

Streptomyces peucetius var. caesius is an aerobic bacterium that produces doxorubicin as a secondary metabolite. A mixture design was applied for the screening of suitable complex medium components in the cultivation of S. peucetius var. caesius N47, which is an epsilon-rhodomycinone-accumulating mutant strain. epsilon-Rhodomycinone is a non-glycosylated precursor of doxorubicin. Best growth results were obtained with soy peptone and beef extract. A central composite face-centered (CCF) experimental design was constructed for the investigation of pH, temperature and dissolved oxygen (DO) effects on the cultivation growth phase. Another CCF was applied to the production phase to investigate the effects of aeration, pH, temperature and stirring rate on epsilon-rhodomycinone production. An increase in cultivation temperature increased both cell growth and glucose consumption rate. Best epsilon-rhodomycinone productivities were obtained in temperatures around 30 degrees C. DO control increased all growth phase responses, but aeration in the production phase coupled with pH decrease resulted in rapid epsilon-rhodomycinone decay in the medium. In non-aerated production phases a pH change resulted in better productivity than in experiments without pH change. A pH increase with a temperature decrease seemed most beneficial for productivity. This implies that dynamic control strategies in batch production of epsilon-rhodomycinone could increase the overall process productivity.

Light sensitivity of Bifidobacterium longum in bioreactor cultivations.

Bifidobacteria are gaining commercial significance due to their probiotic properties. However, little is still known about the production of these bacteria and their behavior in bioreactors. Two Bifidobacterium longum strains were sensitive to light when grown in a transparent (glass) bioreactor under microaerophilic growth conditions (i.e. no gases added and slow mixing). The sensitivity was less clear the more anaerobic the initial conditions were. In a darkened bioreactor in microaerophilic conditions, the two strains grew with maximum specific growth rates of 0.36 h(-1) and 0.48 h(-1). In an illuminated bioreactor neither strain grew. In comparison, Lactobacillus reuteri was not sensitive to light under the same conditions.

Improved xylanase production by Trichoderma reesei grown on L-arabinose and lactose or D-glucose mixtures.

Trichoderma reesei Rut C-30 was grown on eight different natural or rare aldopentoses as the main carbon source and on mixtures of an aldopentose with D-glucose or lactose. The fungal cells consumed all aldopentoses tested, except L-xylose and L-ribose. The highest total xylanase and cellulase activities were achieved when cells were grown on L-arabinose as the main carbon source. The total xylanase activity produced by cells grown on L-arabinose was even higher than that produced by cells grown on an equal amount of lactose. In co-metabolism of D-glucose (15 g l(-1)) and L-arabinose (5 g l(-1)), the total volumetric and specific xylanase productivities were improved (derepressed) approximately 23- and 18-fold, respectively, compared to a cultivation on only D-glucose (20 g l(-1)). In a similar experiment, in which cells were grown on a mixture of lactose and L-arabinose, the xylanase productivity was approximately doubled, compared to a cultivation on only lactose. The cellulase productivities, however, were not improved by the addition of L-arabinose. Compared with a typical industrial fungal enzyme production process with lactose as the main carbon source, better volumetric and specific xylanase productivities were achieved both on a lactose/arabinose mixture and on a glucose/arabinose mixture.

Growth characteristics and oxidative capacity of Acetobacter aceti IFO 3281: implications for L-ribulose production.

We studied the growth characteristics and oxidative capacities of Acetobacter aceti IFO 3281 in batch and chemostat cultures. In batch culture, glycerol was the best growth substrate and growth on ethanol occurred only after 6 days delay, although ethanol was rapidly oxidized to acetic acid. In continuous culture, both glycerol and ethanol were good growth substrates with similar characteristics. Resting cells in a bioreactor oxidized ribitol to L-ribulose with a maximal specific rate of 1.2 g g(-1) h(-1)). The oxidation of ribitol was inhibited by ethanol but not by glycerol. Biomass yield (Y(SX); C-mmol/C-mmol) on ethanol and glycerol was low (0.21 and 0.17, respectively). In the presence of ribitol the yield was somewhat higher (0.25) with ethanol but lower (0.13) with glycerol, with respectively lower and higher CO(2) production. In chemostat cultures the oxidation rate of ribitol was unaffected by ethanol or glycerol. Cell-free extract oxidized ethanol very slowly but not ribitol; the oxidative activity was located in the cell membrane fraction. Enzymatic activities of some key metabolic enzymes were determined from steady-state chemostat with ethanol, glycerol, or ethanol/glycerol mixture as a growth limiting substrate. Based on the measured enzyme activities, metabolic pathways are proposed for ethanol and glycerol metabolism.

High-level production of D-mannitol with membrane cell-recycle bioreactor.

Ten heterofermentative lactic acid bacteria were compared in their ability to produce D-mannitol from D-fructose in a resting state. The best strain, Leuconostoc mesenteroides ATCC-9135, was examined in high cell density membrane cell-recycle cultures. High volumetric mannitol productivity (26.2 g l(-1) h(-1)) and mannitol yield (97 mol%) were achieved. Using the same initial biomass, a stable high-level production of mannitol was maintained for 14 successive bioconversion batches. Applying response surface methodology, the temperature and pH were studied with respect to specific mannitol productivity and yield. Moreover, increasing the initial fructose concentration from 100 to 120 and 140 g l(-1) resulted in decreased productivities due to both substrate and end-product inhibition of the key enzyme, mannitol dehydrogenase (MDH). Nitrogen gas flushing of the bioconversion media was unnecessary, since it did not change the essential process parameters.

Controlled transient changes reveal differences in metabolite production in two Candida 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.

Actinopolyspora halophila has two separate pathways for betaine synthesis.

The extremely halophilic actinomycete Actinopolyspora halophila is a rare example of a heterotrophic eubacterium producing betaine from simple carbon sources. A. halophila synthesized remarkably high intracellular concentrations of betaine. The highest betaine concentration, determined at 24% (w/v) NaCl, was 33% of the cellular dry weight. Trehalose was synthesized as a compatible solute, accounting for up to 9.7% of the cellular dry weight. The betaine concentration was shown to increase with increasing NaCl concentration, whereas the trehalose concentration was highest at the lowest NaCl concentration used (15% w/v). A. halophila was capable of accumulating betaine from the medium, while at the same time betaine was also excreted back into the medium by the cells. Along with the de novo synthesis of betaine, A. halophila was able to take up choline from the medium and oxidize it to betaine. Some basic characteristics of the choline oxidation system are described. Choline was oxidized to betaine aldehyde in a reaction in which H2O2 generation and oxygen consumption were coupled. Betaine aldehyde was also oxidized, but with lesser efficiency. In addition, betaine aldehyde was oxidized further to betaine in a reaction in which NAD(P)+ was reduced.

Optimisation of media and cultivation conditions for L(+)(S)-lactic acid production by Lactobacillus casei NRRL B-441.

Process variables and concentration of carbon in media were optimised for lactic acid production by Lactobacillus casei NRRL B-441. Lactic acid yield was inversely proportional to initial glucose concentration within the experimental area (80-160 g l(-1)). The highest lactic acid concentration in batch fermentation, 118.6 g l(-1), was obtained with 160 g 1(-1) glucose. The maximum volumetric productivity, 4.4 g 1(-1) h(-1) at 15 h, was achieved at an initial glucose concentration of 100 g l(-1). Similar lactic acid concentrations were reached with a fedbatch approach using growing cells, in which case the fermentation time was much shorter. Statistical experimental design and response surface methodology were used for optimising the process variables. The temperature and pH optima for lactic acid production were 35 degrees C, pH 6.3. Malt sprout extract supplemented with yeast extract (4 g l(-1)) appeared to be an economical alternative to yeast extract alone (22 g l(-1)) although the fermentation time was a little longer. The results demonstrated both the separation of the growth and lactic acid production phases and lactic acid production by non-growing cells without any nutrient supplements. Resting L. casei cells converted 120 g l(-1) glucose to lactic acid with 100% yield and a maximum volumetric productivity of 3.5 g l(-1) h(-1).

A combination of weakly stabilizing mutations with a disulfide bridge in the alpha-helix region of Trichoderma reesei endo-1,4-beta-xylanase II increases the thermal stability through synergism.

Thermal stability and other functional properties of Trichoderma reesei endo-1,4-beta-xylanase II (XYNII; family 11) were studied by designed mutations. Mutations at three positions were introduced to the XYNII mutant containing a disulfide bridge (S110C-N154C) in the alpha-helix. The disulfide bridge increased the half-life of XYNII from less than 1 min to 14 min at 65 degrees C. An additional mutation at the C-terminus of the alpha-helix (Q162H or Q162Y) increased the half-life to 63 min. Mutations Q162H and Q162Y alone had a stabilizing effect at 55 degrees C but not at 65 degrees C. The mutations N11D and N38E increased the half-life to about 100 min. Due to the stabilizing mutations the pH stability increased in a wide pH range, but at the same time the activity decreased both in acidic and neutral-alkaline pH, the pH optimum being at pH region 5-6. There was no essential difference between the specific activities of the mutants and the wild-type XYNII.

Improved osmotolerance of recombinant Escherichia coli by de novo glycine betaine biosynthesis.

The genes from the extreme halophile Ecto-thiorhodospira halochloris encoding the biosynthesis of glycine betaine from glycine were cloned into Escherichia coli. The accumulation of glycine betaine and its effect on osmotolerance of the cells were studied. In mineral medium with NaCl concentrations from 0.15 to 0.5 M, the accumulation of both endogenously synthesized and exogenously provided glycine betaine stimulated the growth of E. coli. The intracellular levels of glycine betaine and the cellular yields were clearly higher for cells receiving glycine betaine exogenously than for cells synthesizing it. The lower level of glycine betaine accumulation in cells synthesizing it is most likely a consequence of the limited availability of precursors (e.g. S-adenosylmethionine) rather than the result of a low expression level of the genes. Glycine betaine also stimulated the growth of E. coli and decreased acetate formation in mineral medium with high sucrose concentrations (up to 200 g.l(-1)).

Thermostability of endo-1,4-beta-xylanase II from Trichoderma reesei studied by electrospray ionization Fourier-transform ion cyclotron resonance MS, hydrogen/deuterium-exchange reactions and dynamic light scattering.

Endo-1,4-beta-xylanase II (XYNII) from Trichoderma reesei is a 21 kDa enzyme that catalyses the hydrolysis of xylan, the major plant hemicellulose. It has various applications in the paper, food and feed industries. Previous thermostability studies have revealed a significant decrease in enzymic activity of the protein at elevated temperatures in citrate buffer [Tenkanen, Puls and Poutanen (1992) Enzyme Microb. Technol. 14, 566-574]. Here, thermostability of XYNII was investigated using both conventional and nanoelectrospray ionization Fourier-transform ion cyclotron resonance MS and hydrogen/deuterium (H/D)-exchange reactions. In addition, dynamic light scattering (DLS) was used as a comparative method to observe possible changes in both tertiary and quaternary structures of the protein. We observed a significant irreversible conformational change and dimerization when the protein was exposed to heat. H/D exchange revealed two distinct monomeric protein populations in a narrow transition temperature region. The conformational change in both the water and buffered solutions occurred in the same temperature region where enzymic-activity loss had previously been observed. Approx. 10-30% of the protein was specifically dimerized when exposed to the heat treatment. However, adding methanol to the solution markedly lowered the transition temperature of conformational change as well as increased the dimerization up to 90%. DLS studies in water confirmed the change in conformation observed by electrospray ionization MS. We propose that the conformational change is responsible for the loss of enzymic activity at temperatures over 50 degrees C and that the functioning of the active site in the enzyme is unfeasible in a new, more labile solution conformation.

Characterization of glycine sarcosine N-methyltransferase and sarcosine dimethylglycine N-methyltransferase.

Glycine betaine is accumulated in cells living in high salt concentrations to balance the osmotic pressure. Glycine sarcosine N-methyltransferase (GSMT) and sarcosine dimethylglycine N-methyltransferase (SDMT) of Ectothiorhodospira halochloris catalyze the threefold methylation of glycine to betaine, with S-adenosylmethionine acting as the methyl group donor. These methyltransferases were expressed in Escherichia coli and purified, and some of their enzymatic properties were characterized. Both enzymes had high substrate specificities and pH optima near the physiological pH. No evidence of cofactors was found. The enzymes showed Michaelis-Menten kinetics for their substrates. The apparent K(m) and V(max) values were determined for all substrates when the other substrate was present in saturating concentrations. Both enzymes were strongly inhibited by the reaction product S-adenosylhomocysteine. Betaine inhibited the methylation reactions only at high concentrations.

Chemostat study of xylitol production by Candida guilliermondii.

The mechanism of production of xylitol from xylose by Candida guilliermondii was studied using chemostat cultures and enzymatic assays. The maximum dilution rate in aerobic conditions was 0.34 1/h. No xylitol was produced. Under oxygen-limited conditions xylose uptake was impaired and glycerol accumulated but no xylitol was detected. Under transient oxygen limitation, caused by a gradual decrease in the agitation rate, onset of xylitol, acetate and residual xylose accumulation occurred simultaneously when qo2 dropped below 25 mmol/C-mmol cell dry weight (CDW) per hour. Ethanol and glycerol started to accumulate when qo2 dropped below 20 mmol/C-mmol CDW per hour. The highest in vitro enzyme activities were found at the lowest dilution rate studied (0.091/h) under aerobic conditions. The amount of active enzymes or cofactor availability did not limit the rate of xylose consumption. Our results confirm that a surplus of NADH during transient oxygen limitation inhibited the activity of xylitol dehydrogenase which resulted in xylitol accumulation. Phosphoglucoisomerase (E.C. 5.3.1.9.) and glucose-6-phosphate dehydrogenase (E.C. 1.1.1.49) activities suggest re-shuttling of the metabolites into the pentose phosphate pathway.

Simultaneous catalysis and product separation by cross-linked enzyme crystals.

Crystalline cross-linked xylose isomerase (CLXI, EC 5.3.1.5) and xylanase (CLX, EC 3.2.1.8) were studied in a packed-bed reactor for simultaneous catalytic reaction and separation of substrates from reaction products. Streptomyces rubiginosus xylose isomerase catalyzed a slow isomerization of L-arabinose to L-ribulose and an epimerization to L-ribose. In equilibrium the reaction mixture contained 52.5% arabinose, 22.5% ribulose, and 25% ribose. In a packed-bed column filled with CLXI, a simultaneous reaction and separation resulted in fractions where arabinose concentration varied between 100-0%, ribulose between 0-55%, and ribose between 0-100%. Trichoderma reesei xylanase II hydrolyzed and transferred xylotetraose mainly to xylotriose and xylobiose. In a packed-bed column filled with CLX, xylotetraose rapidly reacted to xylobiose and xylose by a mechanism that is not yet fully understood.