Xylose-grown Cells Research Articles

Proteome analysis of xylose metabolism in Rhodotorula toruloides during lipid production

BackgroundRhodotorula toruloides is a promising platform organism for production of lipids from lignocellulosic substrates. Little is known about the metabolic aspects of lipid production from the lignocellolosic sugar xylose by oleaginous yeasts in general and R. toruloides in particular. This study presents the first proteome analysis of the metabolism of R. toruloides during conversion of xylose to lipids.ResultsRhodotorula toruloides cultivated on either glucose or xylose was subjected to comparative analysis of its growth dynamics, lipid composition, fatty acid profiles and proteome. The maximum growth and sugar uptake rate of glucose-grown R. toruloides cells were almost twice that of xylose-grown cells. Cultivation on xylose medium resulted in a lower final biomass yield although final cellular lipid content was similar between glucose- and xylose-grown cells. Analysis of lipid classes revealed the presence of monoacylglycerol in the early exponential growth phase as well as a high proportion of free fatty acids. Carbon source-specific changes in lipid profiles were only observed at early exponential growth phase, where C18 fatty acids were more saturated in xylose-grown cells. Proteins involved in sugar transport, initial steps of xylose assimilation and NADPH regeneration were among the proteins whose levels increased the most in xylose-grown cells across all time points. The levels of enzymes involved in the mevalonate pathway, phospholipid biosynthesis and amino acids biosynthesis differed in response to carbon source. In addition, xylose-grown cells contained higher levels of enzymes involved in peroxisomal beta-oxidation and oxidative stress response compared to cells cultivated on glucose.ConclusionsThe results obtained in the present study suggest that sugar import is the limiting step during xylose conversion by R. toruloides into lipids. NADPH appeared to be regenerated primarily through pentose phosphate pathway although it may also involve malic enzyme as well as alcohol and aldehyde dehydrogenases. Increases in enzyme levels of both fatty acid biosynthesis and beta-oxidation in xylose-grown cells was predicted to result in a futile cycle. The results presented here are valuable for the development of lipid production processes employing R. toruloides on xylose-containing substrates.

Carbohydrate catabolism in Phaeobacter inhibens DSM 17395, a member of the marine roseobacter clade.

Since genome analysis did not allow unambiguous reconstruction of transport, catabolism, and substrate-specific regulation for several important carbohydrates in Phaeobacter inhibens DSM 17395, proteomic and metabolomic analyses of N-acetylglucosamine-, mannitol-, sucrose-, glucose-, and xylose-grown cells were carried out to close this knowledge gap. These carbohydrates can pass through the outer membrane via porins identified in the outer membrane fraction. For transport across the cytoplasmic membrane, carbohydrate-specific ABC transport systems were identified. Their coding genes mostly colocalize with the respective "catabolic" and "regulatory" genes. The degradation of N-acetylglucosamine proceeds via N-acetylglucosamine-6-phosphate and glucosamine-6-phosphate directly to fructose-6-phosphate; two of the three enzymes involved were newly predicted and identified. Mannitol is catabolized via fructose, sucrose via fructose and glucose, glucose via glucose-6-phosphate, and xylose via xylulose-5-phosphate. Of the 30 proteins predicted to be involved in uptake, regulation, and degradation, 28 were identified by proteomics and 19 were assigned to their respective functions for the first time. The peripheral degradation pathways feed into the Entner-Doudoroff (ED) pathway, which is connected to the lower branch of the Embden-Meyerhof-Parnas (EMP) pathway. The enzyme constituents of these pathways displayed higher abundances in P. inhibens DSM 17395 cells grown with any of the five carbohydrates tested than in succinate-grown cells. Conversely, gluconeogenesis is turned on during succinate utilization. While tricarboxylic acid (TCA) cycle proteins remained mainly unchanged, the abundance profiles of their metabolites reflected the differing growth rates achieved with the different substrates tested. Homologs of the 74 genes involved in the reconstructed catabolic pathways and central metabolism are present in various Roseobacter clade members.

Harnessing Candida tenuis and Pichia stipitis in whole‐cell bioreductions of o‐chloroacetophenone: Stereoselectivity, cell activity, in situ substrate supply and product removal

Generally, recombinant and native microorganisms can be employed as whole-cell catalysts. The application of native hosts, however, shortens the process development time by avoiding multiple steps of strain construction. Herein, we studied the NAD(P)H-dependent reduction of o-chloroacetophenone by isolated xylose reductases and their native hosts Candida tenuis and Pichia stipitis. The natural hosts were benchmarked against Escherichia coli strains co-expressing xylose reductase and a dehydrogenase for co-enzyme recycling. Xylose-grown cells of C. tenuis and P. stipitis displayed specific o-chloroacetophenone reductase activities of 366 and 90 U gCDW (-1) , respectively, in the cell-free extracts. Fresh biomass was employed in batch reductions of 100 mM o-chloroacetophenone using glucose as co-substrate. Reaction stops at a product concentration of about 15 mM, which suggests sensitivity of the catalyst towards the formed product. In situ substrate supply and product removal by the addition of 40% hexane increased catalyst stability. Optimisation of the aqueous phase led to a (S)-1-(2-chlorophenyl)ethanol concentration of 71 mM (ee > 99.9%) obtained with 44 gCDW L(-1) of C. tenuis. The final difference in productivities between native C. tenuis and recombinant E. coli was < 1.7-fold. The optically pure product is a required key intermediate in the synthesis of a new class of chemotherapeutic substances (polo-like kinase 1 inhibitors).

Culture nutrition and physiology impact the inhibitor tolerance of the yeastPichia stipitisNRRL Y‐7124

Pichia stipitis NRRL Y-7124 is one of the natural yeasts best able to utilize biomass because it is able to ferment hexoses and the pentose, xylose, to economically recoverable concentrations of ethanol. To test the impact of culture conditions on inhibitor tolerance, inhibitors were spiked to growing or stationary-phase P. stipitis supplied either glucose or xylose and varying nitrogen and mineral compositions; then the ensuing specific death rate response was measured. Resistance of glucose- or xylose-grown cells to inhibitors was generally greater in stationary-phase cells than log-phase cells, despite a greater exposure of stationary cells to ethanol. Consistent with this, the specific productivity of detoxification products, furan methanol or furan-2,5-dimethanol, from respective spikes of furfural or HMF increased as cultures progressed into stationary phase. However, when xylose was the substrate, ethanol resistance behaved uniquely and was greater for log- than stationary-phase cells. Amino acid enrichment of the growth medium significantly enhanced ethanol tolerance if xylose was the carbon source, but had no impact if glucose supplied carbon. Regardless of the carbon source, amino acid enrichment of the culture medium enhanced the ability of cells to resist furfural and HMF exposure. Mineral compositions tested had little impact on inhibitor resistance except stationary-phase xylose-grown cells were more susceptible to inhibitor exposure when magnesium sulfate was excessive. Observed tolerance optimization based on specific death rate as a function of culture physiological state, carbon source, nitrogen source and mineral composition provides new knowledge supporting process designs to convert biomass to ethanol using P. stipitis.

Novel xylose dehydrogenase in the halophilic archaeon Haloarcula marismortui.

During growth of the halophilic archaeon Haloarcula marismortui on D-xylose, a specific D-xylose dehydrogenase was induced. The enzyme was purified to homogeneity. It constitutes a homotetramer of about 175 kDa and catalyzed the oxidation of xylose with both NADP+ and NAD+ as cosubstrates with 10-fold higher affinity for NADP+. In addition to D-xylose, D-ribose was oxidized at similar kinetic constants, whereas D-glucose was used with about 70-fold lower catalytic efficiency (kcat/Km). With the N-terminal amino acid sequence of the subunit, an open reading frame (ORF)-coding for a 39.9-kDA protein-was identified in the partially sequenced genome of H. marismortui. The function of the ORF as the gene designated xdh and coding for xylose dehydrogenase was proven by its functional overexpression in Escherichia coli. The recombinant enzyme was reactivated from inclusion bodies following solubilization in urea and refolding in the presence of salts, reduced and oxidized glutathione, and substrates. Xylose dehydrogenase showed the highest sequence similarity to glucose-fructose oxidoreductase from Zymomonas mobilis and other putative bacterial and archaeal oxidoreductases. Activities of xylose isomerase and xylulose kinase, the initial reactions of xylose catabolism of most bacteria, could not be detected in xylose-grown cells of H. marismortui, and the genes that encode them, xylA and xylB, were not found in the genome of H. marismortui. Thus, we propose that this first characterized archaeal xylose dehydrogenase catalyzes the initial step in xylose degradation by H. marismortui.

Metabolic analysis of acetate accumulation during xylose consumption by Paenibacillus polymyxa.

Paenibacillus polymyxa ATCC 12321 produced more acetic acid and less butanediol from xylose than from glucose. The product yields from xylose were ethanol (0.72 mol/mol sugar), (R,R)-2,3-butanediol (0.31 mol/mol sugar), and acetate (0.38 mol/mol sugar) while those from glucose were ethanol (0.74 mol/mol sugar), (R,R)-2,3-butanediol (0.46 mol/mol sugar), and acetate (0.05 mol/mol sugar). Higher acetate kinase activity and lower acetate uptake ability were found in xylose-grown cells than in glucose-grown cells. Furthermore, phosphoketolase activity was higher in xylose-grown cells than in glucose-grown cells. In fed-batch culture on xylose, glucose feeding raised the butanediol yield to 0.56 mol/mol sugar and reduced acetate accumulation to 0.04 mol/mol sugar.

Cloning and transcriptional analysis of the Thermoanaerobacter ethanolicus strain 39E maltose ABC transport system.

Thermoanaerobacter ethanolicus strain 39E is a Gram-positive thermophile that converts sugars resulting from plant carbohydrate polymer degradation into ethanol. A putative maltose ATP-binding cassette (ABC) transport operon was isolated with genes encoding for the integral membrane components (malF and malG); the ATP-binding protein (malK); and a partial gene for the maltose-binding protein (malE). This operon is unlike most other maltose transport operons, which do not contain a contiguous malK gene. Sequence analysis showed that the individual genes in the putative operon possessed a considerable range of similarities to their respective homologs in other eubacteria and archaea. MalK had 52% amino-acid identity and over 70% similarity with its homolog from the archaeon Thermococcus litoralis, while the membrane components and binding protein exhibited much less similarity with a range of other thermophilic eubacteria. Transcript was not detected in maltose-, glucose-, or xylose-grown cells using Northern blotting, but RT-PCR showed that malFGK were expressed in cells grown on maltose or xylose. Based on these results, the strain 39E maltose operon may be subject to glucose catabolite repression.

Global gene expression differences associated with changes in glycolytic flux and growth rate in Escherichia coli during the fermentation of glucose and xylose.

The simplicity of the fermentation process (anaerobic with pH, temperature, and agitation control) in ethanologenic Escherichia coli KO11 and LY01 makes this an attractive system to investigate the utility of gene arrays for biotechnology applications. By using this system, gene expression, glycolytic flux, and growth rate have been compared in glucose-grown and xylose-grown cells. Although the initial metabolic steps differ, ethanol yields from both sugars were essentially identical on a weight basis, and little carbon was diverted to biosynthesis. Expression of only 27 genes changed by more than 2-fold in both strains. These included induction of xylose-specific operons (xylE, xylFGHR, and xylAB) regulated by XylR and the cyclic AMP-CRP system and repression of Mlc-regulated genes encoding glucose uptake (ptsHIcrr, ptsG) and mannose uptake (manXYZ) during growth on xylose. However, expression of genes encoding central carbon metabolism and biosynthesis differed by less than 2-fold. Simple statistical methods were used to investigate these more subtle changes. The reproducibility (coefficient of variation of 12%) of expression measurements (mRNA as cDNA) was found to be similar to that typically observed for in vitro measurements of enzyme activities. Using Student's t test, many smaller but significant sugar-dependent changes were identified (p < 0.05 in both strains). A total of 276 genes were more highly expressed during growth on xylose; 307 genes were more highly expressed with glucose. Slower growth (lower ATP yield) on xylose was accompanied by decreased expression of 62 genes concerned with the biosynthesis of small molecules (amino acids, nucleotides, cofactors, and lipids), transcription, and translation; 5 such genes were expressed at a higher level. In xylose-grown cells, 90 genes associated with the transport, catabolism, and regulation of pathways for alternative carbon sources were expressed at higher levels than in glucose-grown cells, consistent with a relaxation of control by the cyclic AMP-CRP regulatory system. Changes in expression of genes encoding the Embden-Meyerhof-Parnas (EMP) pathway were in excellent agreement with calculated changes in flux for individual metabolites. Flux through all but one step, pyruvate kinase, was predicted to be higher during glucose fermentation. Expression levels (glucose/xylose) were higher in glucose-grown cells for all EMP genes except the isoenzymes encoding pyruvate kinase (pykA and pykF). Expression of both isoenzymes was generally higher during xylose fermentation but statistically higher in both strains only for pykF encoding the isoenzyme activated by fructose-6-phosphate, a key metabolite connecting pentose metabolism to the EMP pathway. The coordinated changes in expression of genes encoding the EMP pathway suggest the presence of a common regulatory system and that flux control within the EMP pathway may be broadly distributed. In contrast, expression levels for genes encoding the Pentose-Phosphate pathway did not differ significantly between glucose-grown and xylose-grown cells.

Petrotoga mobilis sp. nov., from a North Sea oil-production well.

Rod-shaped, thermophilic bacteria with a sheath-like outer structure (toga) were isolated from hot oilfield water of a North Sea oil reservoir. One of the isolates, designated SJ95(T), is an obligately anaerobic, sheathed, Gram-negative, fermentative bacterium capable of reducing elemental sulfur to hydrogen sulfide and tolerating high salt concentrations. The optimum growth conditions for this isolate are 58-60 degrees Celsius and pH 6.5-7.0 with 3-4% NaCl and 0.7% MgSO(4). 7H(2)O in the medium. Vitamins are required for growth. Growth is stimulated by yeast extract. Cells of strain SJ95(T) vary in size from 1-2 to 40-50 micron in length and are motile with a subpolar flagellation. Cels grown on xylan have xylanase activity, presumably associated with the toga, and glucose isomerase activity was detected in xylose-grown cells. The DNA G+C content is 31 and 34 mol%, determined by the thermal denaturation and HPLC methods, respectively. Phylogenetically, strain SJ95(T) is most closely related to Petrotoga miotherma with a 97.7% similarity level between their 165 rDNA sequences. The DNA-DNA reassociation value between the two DNAs was 35.6%. On the basis of differences in genotypic, phenotypic and immunological characteristics, strain SJ95t (=DSM 10674t) is proposed as the type strain of a new species, Petrotoga mobilis. It can be readily distinguished from P. miotherma by its motility.

Relationship Between Effect of Ethanol on Proton Flux Across Plasma Membrane and Ethanol Tolerance, inPichia stipitis

Pichia stipitisefficiently converts glucose or xylose into ethanol but is inhibited by ethanol concentrations exceeding 30 g/L. InSaccharomyces cerevisiae, ethanol has been shown to alter the movement of protons into and out of the cell. InP. stipitisthe passive entry of protons into either glucose- or xylose-grown cells is unaffected at physiological ethanol concentrations. In contrast, active proton extrusion is affected differentially by ethanol, depending on the carbon source catabolized. In fact, in glucose-grown cells, the H+-extrusion rate is reduced by low ethanol concentrations, whereas, in xylose-grown cells, the H+-extrusion rate is reduced only at non-physiological ethanol concentrations. Thus, the ethanol inhibitory effect on growth and ethanol production, in glucose-grown cells, is probably caused by a reduction in H+-extrusion. Comparison of the rates of H+-flux with the relatedin vitroH+-ATPase activity suggests a new mechanism for the regulation of the proton pumping plasma membrane ATPase (EC 3.6.1.3) ofP. stipitis, by both glucose and ethanol. Glucose activates both the ATP hydrolysis and the proton-pumping activities of the H+-ATPase, whereas ethanol causes an uncoupling between the ATP hydrolysis and the proton-pumping activities. This uncoupling may well be the cause of ethanol induced growth inhibition of glucose grownP. stipitiscells.

Characterization of xylitol dehydrogenase from debaryomyces hansenii

The xylitol dehydrogenase (EC 1.1.1.9) from xylose-grown cells ofDebaryomyces hansenii was partially purified in two Chromatographic steps, and characterization studies were carried out in order to inves tigate the role of the xylitol dehydrogenase-catalyzed step in the regu lation of D-xylose metabolism. The enzyme was most active at pH 9.0–9.5, and exhibited a broad polyol specificity. The Michaelis con stants for xylitol and NAD+ were 16.5 and 0.55 mM, respectively. Ca2+, Mg2+, and Mn2+ did not affect the enzyme activity. Conversely, Zn2+, Cd2+, and Co2+ strongly inhibited the enzyme activity. It was concluded that NAD+-xylitol dehydrogenase from D.hansenii has similarities with other xylose-fermenting yeasts in respect to optimal pH, substrate specificity, and Km value for xylitol, and therefore should be named L-iditol:NAD+-5-oxidoreductase (EC 1.1.1.14). The reason D.hansenii is a good xylitol producer is not because of its value of Km for xylitol, which is low enough to assure its fast oxidation by NAD+ xylitol dehydrogenase. However, a higher Km value of xylitol dehydro genase for NAD+ compared to theK m values of other xylose-ferment ing yeasts may be responsible for the higher xylitol yields.

Influence of external electron acceptors and of CO and H2 on the xylose metabolism ofBacteroides xylanolyticus X5.1

WhenBacteroides xylanolyticus X5-1 was grown on xylose in batch culture, acetate, ethanol, H2, CO2 and formate were the main fermentation products. CO inhibited H2 formation byB. xylanolyticus X5-1. As a result, the product formation shifted to more ethanol and formate and less acetate. Furthermore, less biomass was produced. H2 had almost no effect on the product formation from xylose. In batch cultures, dihydroxyacetone, acetone, acetoin and acetol could act as electron acceptors during xylose metabolism. The electron acceptors were reduced to their corresponding alcohols. The product formation from xylose byB. xylanolyticus X5-1 shifted to mainly acetate and CO2, and an increased biomass yield was obtained. H2, ethanol and formate were no longer produced. In continuous cultures not only 1,2-propanediol was formed from acetol, but also acetone. The NADP-dependent ethanol dehydrogenase that was present in xylosegrown continuous-culture cells, was repressed when the organism was grown in the presence of acetol. However, another alcohol dehydrogenase was induced for reduction of the external electron acceptor.

Purification and properties of xylitol dehydrogenase from the xylose-fermenting yeastCandida shehatae

Xylitol dehydrogenase (EC1.1.1.9) from xylose-grown cells ofCandida shehatae was purified 215-fold by sequential chromatography on NAD-C8 affinity, Superose-12, and Cibacron blue columns, and a single band was observed by SDS gel electrophoresis. The purified enzyme had a native molecular weight of 82 kDa and a denatured molecular weight of 40 kDa following SDS gel electrophoresis, indicating that it was composed of two subunits. Alcohol dehydrogenase copurified on the NAD-C8 but was substantially removed by Superose-12 and was not detected following Cibacron blue chromatography. The kinetic properties of the C.shehatae xylitol dehydrogenase differed considerably from those described previously for thePachysolen tannophilus enzyme. The Km of the C.shehatae enzyme for xylitol was 3.8 times smaller, whereas the Km for xylulose was 1.7-fold bigger. These factors could account for the lower xylitol production by C.shehatae.

Characterization of Thermoanaerobacter Glucose Isomerase in Relation to Saccharidase Synthesis and Development of Single-Step Processes for Sweetener Production

Regulation of glucose isomerase synthesis was studied in Thermoanaerobacter strain B6A, which fermented a wide variety of carbohydrates including glucose, xylose, lactose, starch, and xylan. Glucogenic amylase activities and beta-galactosidase were produced constitutively, whereas the synthesis of glucose isomerase was induced by either xylose or xylan. Production of these saccharidase activities was not significantly repressed by the presence of glucose or 2-deoxyglucose in the growth media. Glucose isomerase production was optimized by controlling the culture pH at 5.5 during xylose fermentation. The apparent temperature and pH optima for these cell-bound saccharidase activities were as follows: glucose isomerase, 80 degrees C, pH 7.0 to 7.5; glucogenic amylase, 70 degrees C, pH 5.0 to 5.5; and beta-galactosidase, 60 degrees C, pH 6.0 to 6.5 Glucose isomerase, glucogenic amylase, and beta-galactosidase were produced in xylose-grown cells that were active and stable at 60 to 70 degrees C and pH 6.0 to 6.5. Under single-step process conditions, these saccharidase activities in whole cells or cell extracts converted starch or lactose directly into fructose mixtures. A total of 96% of initial liquefied starch was converted into a 49:51 mixture of glucose and fructose, whereas 85% of initial lactose was converted into a 40:31:29 mixture of galactose, glucose, and fructose.

Levels of pentose phosphate pathway enzymes fromCandida shehatae grown in continuous culture

Candida shehatae exhibits different fermentative capacities when grown under different aeration conditions. These studies investigated the titers of xylose reductase, xylitol dehydrogenase, glucose-6-phosphate dehydrogenase and alcohol dehydrogenase in crude extracts ofCandida shehatae grown in continuous culture with various specific aeration rates. Carbon source, aeration rate, dilution rate and temperature were examined as variables. Xylose reductase and xylitol dehydrogenase were induced by xylose and were largely absent in glucose-grown cells. Alcohol dehydrogenae levels were higher in glucose-grown cells than in xylose-grown cells. The levels of this enzyme also correlated with the fermentative character of metabolism, having a low value under fully aerobic conditions, a high value under anaerobic conditions, and intermediate levels under various semi-aerobic conditions. Temperature had no effect on any enzyme level over the range of 20–30°C.

Purification and Characterization of Xylose Isomerase of a Methanol Yeast,Candida boidinii, Which is Involved in Sorbitol Production from Glucose

d-Xylose (xylose) isomerase was extracted from xylose-grown cells of a methanol yeast, Candida boidinii (Kloeckera sp.) No. 2201. The enzyme was purified 70-fold, over the original cell- free extract, with a yield of 2.4% in a homogeneous state, as judged on sodium dodecyl sulfate- polyacrylamide gel electrophoresis and high performance liquid chromatography. The molecular weight of the enzyme was determined to be 130,000, the enzyme being composed of two subunits of 65,000. The optimum pH and temperature for activity were 4.5 and 37~45°C, respectively. The enzyme activity was markedly enhanced by Mn2+, Mg2+ and Co2+, and the enzyme isomerized aldopentoses and aldohexoses. The Km values for xylose and d-glucose were 5.6 × 10−1m and 4.1 × 10−1m, and the Vmax values were 5.8 × 102 and 3.3 × 102 µmol/min/mg, respectively. NaHAsO4 7H2O and NaCN strongly inhibited the activity, but HgCl2, NaN3, dithiothreitol, monoiodoacetate and polyols such as d-sorbitol, xylitol and d-mannitol did not inhibit the activity.

Purification and characterization of xylose isomerase of a methanol yeast, Candida boidinii, which is involved in sorbitol production from glucose.

d-Xylose (xylose) isomerase was extracted from xylose-grown cells of a methanol yeast, Candida boidinii (Kloeckera sp.) No. 2201. The enzyme was purified 70-fold, over the original cell- free extract, with a yield of 2.4% in a homogeneous state, as judged on sodium dodecyl sulfate- polyacrylamide gel electrophoresis and high performance liquid chromatography. The molecular weight of the enzyme was determined to be 130,000, the enzyme being composed of two subunits of 65,000. The optimum pH and temperature for activity were 4.5 and 37~45°C, respectively. The enzyme activity was markedly enhanced by Mn2+, Mg2+ and Co2+, and the enzyme isomerized aldopentoses and aldohexoses. The Km values for xylose and d-glucose were 5.6 × 10−1m and 4.1 × 10−1m, and the Vmax values were 5.8 × 102 and 3.3 × 102 µmol/min/mg, respectively. NaHAsO4 7H2O and NaCN strongly inhibited the activity, but HgCl2, NaN3, dithiothreitol, monoiodoacetate and polyols such as d-sorbitol, xylitol and d-mannitol did not inhibit the activity.

Molecular expression of xylanase gene in Cryptococcus albidus

In the yeast Cryptococcus albidus, the utilization of xylan as compared to xylose requires at least an inducible endoxylanase enzyme, secreted in the culture medium. The endoxylanase induction was monitored by immunoprecipitation of in vivo and in vitro synthesized products. The mature endoxylanase is a highly glycosylated enzyme with an apparent molecular weight of 48000. Upon chemical deglycosylation with trifluoromethanesulfonic acid, the molecular weight was reduced to 40000. Addition of tunicamycin to the culture medium resulted in the synthesis of a modified polypeptide having a molecular weight of 40000. Poly(A)-containing RNA isolated from the yeast was translated in the rabbit reticulocyte protein-synthesizing system. The appearance of a translatable xylanase mRNA was observed in xylan-grown cells but not in xylose-grown cells. The polypeptide identified as xylanase had a molecular weight of 44000. This suggests that the xylanase is synthesized as a precursor, containing a peptide signal sequence of 35 residues.

Regulation and butanol inhibition of D-xylose and D-glucose uptake in Clostridium acetobutylicum.

Clostridium acetobutylicum exhibited diauxie growth in the presence of mixtures of glucose and xylose. Both glucose- and xylose-grown cells had a glucose uptake activity. On the other hand, growth on xylose was associated with the induction of a xylose permease activity, which was repressed by glucose in xylose-induced cells. The rate of sugar uptake with increasing sugar concentrations showed saturation kinetics with an apparent Km of 1.25 X 10(-5) M for glucose and 5 X 10(-3) M for xylose. Concomitant with the production of solvents, the activities of the glucose and xylose transport systems decreased. Among the main products of fermentation, butanol was shown to be a potent inhibitor of the growth of the organism and of the rate of sugar uptake as well as of sugar incorporation into cell materials. These inhibitory effects of butanol were more pronounced in xylose-grown cells than in glucose-grown cells. Butanol completely inhibited growth at a concentration of 14 g/liter for cultures growing on glucose and 8 g/liter for cultures growing on xylose. Concentrations of 7 and 10.5 g/liter of butanol caused a 50% inhibition of the xylose and glucose incorporations into cell materials. These inhibitory levels of butanol were found in typical glucose or xylose fermentation.

A comparison of the oleaginous yeast, Candida curvata, grown on different carbon sources in continuous and batch culture.

The oleaginous yeast, Candida curvata D, was grown in both batch and continuous culture on 5 different carbon sources to compare the efficiency of fat production from the various substrates. Maximum lipid accumulation occurred in batch culture with xylose as the carbon source on nitrogen-limited medium reaching a level of 49% (w/w) of the biomass, but this was reduced to 37% at the optimum dilution rate (D = 0.05/hr) in a chemostat. Both the highest biomass and lipid yields were attained in continuous culture with lactose as the sole carbon source at a dilution rate of D = 0.04/hr, giving an efficiency of substrate conversion of 60 g of biomass and 18.6 g lipid per 100 g lactose utilized. The relative proportions of the major fatty acids (16:0, 18:0, 18:1, 18:2) in the lipid were found to vary considerably in batch culture and in continuous culture under carbon-limited conditions. However, on nitrogen-limited media in the chemostat, the fatty acid composition remained relatively constant over the whole range of dilution rates employed. Lipid from xylose-grown cells contained the greatest percentage of stearic acid (18:0) 15% and the lowest linoleic acid (18:2) 4%, whereas lipid from ethanol-grown cells contained elevated levels of oleic acid (18:1) 51% and decreased palmitic acid (16:0) 25%.