Wood degradation by white rot fungi: cytochemical studies using lignin peroxidase-immunoglobulin-gold complexes

Using an anti-lignin peroxidase antiserum-protein A-gold complex, we found lignin peroxidase mainly intracellularly in several white rot fungi colonizing sawdust under laboratory conditions. This enzyme was also present in fungi found in naturally decayed wood. However, in all cases, lignin peroxidase was located mainly inside the fungal cells. Labeled lignin peroxidase did not bind to the lignocellulosic samples tested, with the exception of poplar milled-wood lignin. These results are discussed in relation to the role of lignin peroxidase during wood degradation.

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.

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

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).

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.

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.

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.

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.

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.

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 α-helix region of Trichoderma reesei endo-1,4-β-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.

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.

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)).

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.

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.

Effect of glycine betaine on osmoadaptation of Propionibacterium acidipropionici cultivated in elevated osmolarities

The sensitivity of industrial strains Acetobacter aceti, Gluconobacter frateurii, and Propionibacterium acidipropionici to osmotic stress was studied. Growth of A. aceti and G. frateurii was totally inhibited at 0.4 M NaCl concentration, but P. acidipropionici was able to grow on a medium containing 1.2 M NaCl. Addition of glycine betaine to the medium had no detectable osmoprotective effect on A. aceti and G. frateurii cultivations in elevated NaCl concentrations, but it enabled cells of P. acidipropionici to achieve faster the maximum specific growth rate after the prolonged lag phase and therefore to gain faster the final biomass and product concentrations. The final concentrations of biomass and product of P. acidipropionici were the same as for the cultivations of the bacterium without NaCl and glycine betaine present in the medium. Intracellular accumulation of glycine betaine was detected in P. acidipropionici cells cultivated in the medium containing glycine betaine. The amount accumulated increased with NaCl concentration, suggesting that glycine betaine plays an important role in the osmoadaptation.

Growth characteristics and metabolic flux analysis of Candida milleri

The growth characteristics of the sourdough yeast Candida milleri was studied in a carbon-limited aerobic chemostat culture on defined medium. The effect of glucose, xylose, and glucose-xylose mixture on metabolite production and on key enzyme activities was evaluated. Xylose as a sole carbon source was not metabolized by C. milleri. Glucose as a sole carbon source produced only biomass and carbon dioxide. When a glucose-xylose mixture (125:125 C-mM) was used as a carbon source, a small amount of xylose was consumed and a low concentration of xylitol was produced (7.20 C-mM). Enzymatic assays indicated that C. milleri does not possess xylitol dehydrogenase activity and its xylose reductase is exclusively NADPH-dependent. In glucose medium both NAD(+)- and NADP(+)-dependent aldehyde dehydrogenase activities were found, whereas in a glucose-xylose medium only NADP(+)-dependent aldehyde dehydrogenase activity was detected. The developed metabolic flux analysis corresponded well with the experimentally measured values of metabolite production, oxygen consumption (OUR), and carbon dioxide production (CER). Turnover number in generation and consumption of ATP, mitochondrial and cytosolic NADH, and cytosolic NADPH could be calculated and redox balance was achieved. Constraints were imposed on the flux estimates such that the directionality of irreversible reactions is not violated, and cofactor dependence of the measured enzyme activities were taken into account in constructing the metabolic flux network.

Metabolic engineering of Lactobacillus helveticus CNRZ32 for production of pure L-(+)-lactic acid

Expression of D-(-)-lactate dehydrogenase (D-LDH) and L-(+)-LDH genes (ldhD and ldhL, respectively) and production of D-(-)- and L-(+)-lactic acid were studied in Lactobacillus helveticus CNRZ32. In order to develop a host for production of pure L-(+)-isomer of lactic acid, two ldhD-negative L. helveticus CNRZ32 strains were constructed using gene replacement. One of the strains was constructed by deleting the promoter region of the ldhD gene, and the other was constructed by replacing the structural gene of ldhD with an additional copy of the structural gene (ldhL) of L-LDH of the same species. The resulting strains were designated GRL86 and GRL89, respectively. In strain GRL89, the second copy of the ldhL structural gene was expressed under the ldhD promoter. The two D-LDH-negative strains produced only L-(+)-lactic acid in an amount equal to the total lactate produced by the wild type. The maximum L-LDH activity was found to be 53 and 93% higher in GRL86 and GRL89, respectively, than in the wild-type strain. Furthermore, process variables for L-(+)-lactic acid production by GRL89 were optimized using statistical experimental design and response surface methodology. The temperature and pH optima were 41 degrees C and pH 5.9. At low pH, when the growth and lactic acid production are uncoupled, strain GRL89 produced approximately 20% more lactic acid than GRL86.

Stability of native and cross-linked crystalline glucose isomerase

Stabilities of native and cross-linked crystalline forms of Streptomyces rubiginosus glucose isomerase were compared in buffer and in 45% glucose/fructose solutions. The cross-linked crystalline form of the enzyme was more stable in the presence of substrate while in a buffer solution the native enzyme was more stable. Inactivation of native enzyme in buffer did not obey first-order kinetics but proceeded with a rapid first phase followed by a stable phase. This stabilization is interpreted to be a result of a conformational change in the protein structure. Inactivation of the native enzyme in buffer was directly related to protein precipitation. In the presence of high substrate concentration, the inactivation was related to browning reactions between the enzyme and the reactive sugar, resulting in soluble sugar-protein complexes.

Exopolysaccharide-producing bacteria from sugar beets

Six hundred microorganisms were isolated from sugar beets collected from different parts of Finland to study their slime production. A total of 170 of them produced exopolysaccharides, of which 35% were heteropolysaccharides. The yield of heteropolysaccharides from sucrose was lower than that of dextrans. Five isolates, which were chosen for closer study, were identified as Leuconostoc mesenteroides (two species), Rahnella aquatilis (two species), and Enterobacter amnigenus.

Sensitization to industrial enzymes in enzyme research and production

OBJECTIVES

This study investigated sensitization to industrial enzymes in Finnish enzyme production and in Finnish laboratories.

METHODS

A cross-sectional study was conducted in 2 plants producing industrial enzymes and in their product development and research laboratories. Sensitization to enzymes and environmental allergens was examined by skin prick tests and specific immunoglobulin E determinations (radioallergosorbent test). The employees were interviewed for work-related respiratory symptoms. Altogether 173 employees were examined.

RESULTS

The skin prick test showed 21 employees (12%) to be sensitized to one or more enzymes. Sixteen positive persons also had specific immunoglobulin E. Atopy was distinctly associated with enzyme sensitization. An exposure-response relationship was found for enzyme sensitization and for respiratory symptoms during work. For sensitization, the exposure-response linear trend was statistically significant. It weakened but remained statistically significant after stratification for atopy. For symptoms, likewise, the exposure-response linear trend was statistically significant, and the statistical significance remained after stratification for atopy.

CONCLUSION

The study confirmed that industrial enzymes are potent sensitizers. The handling of dry enzymes in laboratory work may cause sensitization. Sensitization may even follow minute degrees of exposure, such as among office personnel. Atopics are more susceptible to sensitization than nonatopics. Nonatopics are also clearly at risk; the demonstrated exposure-response relationship emphasizes the need for and advantages of proper exposure control.

Enzyme exposure and enzyme sensitisation in the baking industry

OBJECTIVES

To assess the exposure to enzymes and prevalence of enzyme sensitisation in the baking industry.

METHODS

A cross sectional study was conducted in four bakeries, one flour mill, and one crispbread factory. Sensitisation to enzymes, flours, and storage mites was examined by skin prick and radioallergosorbent (RAST) tests. 365 workers were tested. The workers were interviewed for work related respiratory and skin symptoms. Total dust concentrations were measured by a gravimetric method, and the concentration of alpha-amylase in air was measured by a catalytic method. An immunochemical method was used for measuring cellulase and xylanase in air.

RESULTS

Total measured dust concentrations were from 0.1 to 18 mg/m3, with highest values in dough making areas of bakeries. The alpha-amylase concentrations generally followed the total dust concentrations and reached the highest values < 6.6 micrograms/m3 in the same areas. Cellulase and xylanase varied with concentrations < 180 ng/m3 and < 40 ng/m3, respectively, in the flour mill and the crispbread factory. No cellulase, but concentrations of 1-200 ng/m3 xylanase, were found in the bakeries, probably indicating the natural xylanase activity of wheat. 12 workers (8%) in the bakeries, three (5%) in the flour mill, and four (3%) in the crispbread factory were skin prick positive to enzymes. The corresponding percentages of positive reactions to flours were 12%, 5%, and 8%.

CONCLUSIONS

The study confirmed that industrial enzymes in baking used as additives in a powdered form pose a risk of sensitisation. The no effect air concentrations for industrial enzymes are not known. Based on present knowledge, however, lowering exposures and eliminating short and high peaks by technical measures would lower the risk of sensitisation. This would be most effectively accomplished by shifting to non-dusty products.

A New Method for Protein Crystallization Using High Pressure

Crystallization methods for proteins have been the subject of decades of development yet protein crystallization remains the limiting step in structural studies. We present here a new method for protein crystallization--based on the use of high pressure--that enabled us to accelerate dramatically the growth of glucose isomerase crystals. We think this method may have a more general utility.

Molecular analysis of a Phanerochaete chrysosporium lignin peroxidase gene

The basidiomycete fungus Phanerochaete chrysosporium produces a number of extracellular peroxidases which appear to be important for lignin degradation. We present here the isolation and complete nucleotide (nt) sequence of a gene (lpo) coding for lignin peroxidase (LPO), the coding region of which is identical to a lpo cDNA sequence which had previously been described [M. Tien and C.-P.D. Tu, Nature 326 (1987) 520-523]. The deduced amino acid (aa) sequence corresponds to 372 aa residues and the coding region is interrupted by eight short introns that range in size from 50 to 62 nt. Southern blot experiments using the cloned lpo gene as hybridization probe revealed a complex restriction fragment pattern, indicating that there are a number of lpo-related nucleotide sequences present in P. chrysosporium DNA which cross-hybridize. We also present data on the in vivo expression of the lpo genes and show that they are regulated at the RNA level and that the structure of the transcripts as judged from S1 experiments is complex. These data are consistent with the idea that there are a number of related lpo genes in P. chrysosporium which constitute a gene family.