Hyperproduction of Poly-β-Hydroxybutyrate during Exponential Growth of Azotobacter vinelandii UWD

The transformation of Azotobacter vinelandii UW with A. vinelandii 113 DNA resulted in the formation of rifampin-resistant colonies, 13% of which also inherited a previously unrecognized mutation in the respiratory NADH oxidase. These transformants produced colonies with a white-sectored phenotype after prolonged incubation. Cells from these sectors were separated and purified by streaking and were named UWD. The dense white phenotype was due to the production of a large amount of poly-β-hydroxybutyrate during the exponential growth of strain UWD. The polymer accounted for 65 or 75% of the cell dry weight after 24 h of incubation of cultures containing glucose and either ammonium acetate or N₂, respectively, as the nitrogen source. Under the same conditions, strain UW cells contained 22 to 25% poly-β-hydroxybutyrate, but O₂-limited growth was required for these optimal production values. Polymer production was not dependent on O₂ limitation in strain UWD, but the efficiency of conversion of glucose to poly-β-hydroxybutyrate was enhanced in O₂-limited cultures. Conversion efficiencies were >0.25 and 0.33 mg of poly-β-hydroxybutyrate per mg of glucose consumed under vigorous- and low-aeration conditions, respectively, compared with an efficiency of 0.05 achieved by strain UW. Strain UWD, therefore, appeared to from poly-β-hydroxybutyrate under novel conditions, which may be useful in designing new methods for the industrial production of biodegradable plastics.     

The role of oxygen limitation in the formation of poly-β-hydroxybutyrate during batch and continuous culture of Azotobacter beijerinckii

Azotobacter beijerinckii was grown in ammonia-free glucose-mineral salts media in batch culture and in chemostat cultures limited by the supply of glucose, oxygen or molecular nitrogen. In batch culture poly-beta-hydroxybutyrate was formed towards the end of exponential growth and accumulated to about 74% of the cell dry weight. In chemostat cultures little poly-beta-hydroxybutyrate accumulated in organisms that were nitrogen-limited, but when oxygen limited a much increased yield of cells per mol of glucose was observed, and the organisms contained up to 50% of their dry weight of poly-beta-hydroxybutyrate. In carbon-limited cultures (D, the dilution rate,=0.035-0.240h(-1)), the growth yield ranged from 13.1 to 19.8g/mol of glucose and the poly-beta-hydroxybutyrate content did not exceed 3.0% of the dry weight. In oxygen-limited cultures (D=0.049-0.252h(-1)) the growth yield ranged from 48.4 to 70.1g/mol of glucose and the poly-beta-hydroxybutyrate content was between 19.6 and 44.6% of dry weight. In nitrogen-limited cultures (D=0.053-0.255h(-1)) the growth yield ranged from 7.45 to 19.9g/mol of glucose and the poly-beta-hydroxybutyrate content was less than 1.5% of dry weight. The sudden imposition of oxygen limitation on a nitrogen-limited chemostat culture produced a rapid increase in poly-beta-hydroxybutyrate content and cell yield. Determinations on chemostat cultures revealed that during oxygen-limited steady states (D=0.1h(-1)) the oxygen uptake decreased to 100mul h(-1) per mg dry wt. compared with 675 for a glucose-limited culture (D=0.1h(-1)). Nitrogen-limited cultures had CO(2) production values in situ ranging from 660 to 1055mul h(-1) per mg dry wt. at growth rates of 0.053-0.234h(-1) and carbon-limited cultures exhibited a variation of CO(2) production between 185 and 1328mul h(-1) per mg dry wt. at growth rates between 0.035 and 0.240h(-1). These findings are discussed in relation to poly-beta-hydroxybutyrate formation, growth efficiency and growth yield during growth on glucose. We suggest that poly-beta-hydroxybutyrate is produced in response to oxygen limitation and represents not only a store of carbon and energy but also an electron sink into which excess of reducing power can be channelled.     

Formation of poly(hydroxybutyrate-co-hydroxyvalerate) by Azotobacter vinelandii UWD.

Azotobacter vinelandii UWD formed polyhydroxyalkanoate (PHA) copolymers containing beta-hydroxybutyrate and beta-hydroxyvalerate (HV) when grown in a medium containing glucose as the primary C source and valerate (pentanoate) as a precursor. Copolymer was not formed when propionate was added to the glucose medium but was formed when heptanoate, nonanoate, or trans-2-pentenoate was present. Optimal levels of HV were formed when valerate was added at the time of maximum PHA synthesis, although HV incorporation was not dependent on glucose catabolism. HV content in the polymer was increased from 17 to 24 mol% by adding 10 to 40 mM valerate to glucose medium, but HV insertion into the polymer occurred at a fixed rate. Similarly, the addition of valerate to a fed-batch culture of strain UWD in beet molasses in a fermentor produced 19 to 22 g of polymer per liter, containing 8.5 to 23 mol% HV after 38 to 40 h. The synthesis of HV in these cultures also occurred at a fixed rate (2.3 to 2.8 mol% h-1), while the maximum PHA production rate was 1.1 g liter-1 h-1. During synthesis of copolymer in batch or fed-batch culture, the yield from conversion of glucose into PHA (YP/S) remained at maximum theoretical efficiency (greater than or equal to 0.33 g of PHA per g of glucose consumed). Up to 45 mol% C source, but the PHA produced amounted to less than 1 g/liter. The combination of 30 mM valerate as a sole C source and 0.5 mM 4-pentenoate increased the HV content in the polymer to 52 mol%.(ABSTRACT TRUNCATED AT 250 WORDS)     

Formation of poly(hydroxybutyrate-co-hydroxyvalerate) by Azotobacter vinelandii UWD.

Azotobacter vinelandii UWD formed polyhydroxyalkanoate (PHA) copolymers containing beta-hydroxybutyrate and beta-hydroxyvalerate (HV) when grown in a medium containing glucose as the primary C source and valerate (pentanoate) as a precursor. Copolymer was not formed when propionate was added to the glucose medium but was formed when heptanoate, nonanoate, or trans-2-pentenoate was present. Optimal levels of HV were formed when valerate was added at the time of maximum PHA synthesis, although HV incorporation was not dependent on glucose catabolism. HV content in the polymer was increased from 17 to 24 mol% by adding 10 to 40 mM valerate to glucose medium, but HV insertion into the polymer occurred at a fixed rate. Similarly, the addition of valerate to a fed-batch culture of strain UWD in beet molasses in a fermentor produced 19 to 22 g of polymer per liter, containing 8.5 to 23 mol% HV after 38 to 40 h. The synthesis of HV in these cultures also occurred at a fixed rate (2.3 to 2.8 mol% h-1), while the maximum PHA production rate was 1.1 g liter-1 h-1. During synthesis of copolymer in batch or fed-batch culture, the yield from conversion of glucose into PHA (YP/S) remained at maximum theoretical efficiency (greater than or equal to 0.33 g of PHA per g of glucose consumed). Up to 45 mol% C source, but the PHA produced amounted to less than 1 g/liter. The combination of 30 mM valerate as a sole C source and 0.5 mM 4-pentenoate increased the HV content in the polymer to 52 mol%.(ABSTRACT TRUNCATED AT 250 WORDS)     

Growth of Azotobacter vinelandii UWD in Fish Peptone Medium and Simplified Extraction of Poly-beta-Hydroxybutyrate

Azotobacter vinelandii UWD was grown in a fermentor with glucose medium with and without 0.1% fish peptone (FP) in batch and fed-batch cultures for the production of the natural bioplastic poly-beta-hydroxybutyrate (PHB). Strain UWD formed PHB five times faster than cell protein during growth in glucose and NH(4), but PHB synthesis stopped when NH(4) was depleted and nitrogen fixation started. When FP was added to the same medium, PHB accumulated 16 times faster than cell protein, which in turn was inhibited by 40%, and PHB synthesis was unaffected by NH(4) depletion. Thus, FP appeared to be used as a nitrogen source by these nitrogen-fixing cells, which permitted enhanced PHB synthesis, but it was not a general growth stimulator. The addition of FP to the medium led to the production of large, pleomorphic, osmotically sensitive cells that demonstrated impaired growth and partial lysis, with the leakage of DNA into the culture fluid, but these cells were still able to synthesize PHB at elevated rates and efficiency. When FP was continuously present in fed-batch culture, the yield in grams of polymer per gram of glucose consumed was calculated to range from 0.43 g/g, characteristic of nongrowing cells, to an unprecedented 0.65 g/g. Separation of an FP-free growth phase from an FP-containing growth phase in fed-batch culture resulted in better growth of these pleomorphic cells and good production of PHB (yield, 0.32 g/g). The fragility of these cells was exploited in a simple procedure for the extraction of high-molecular-weight PHB. The cells were treated with 1 N aqueous NH(3) (pH 11.4) at 45 degrees C for 10 min. This treatment removed about 10% of the non-PHB mass from the pellet, of which 60 to 77% was protein. The final product consisted of 94% PHB, 2% protein, and 4% nonprotein residual mass. The polymer molecular weight (1.7 x 10 to 2.0 x 10) and dispersity (1.0 to 1.9) were not significantly affected (P = 0.05) by this treatment. In addition, the NH(3) extraction waste could be recycled in the fermentation as a nitrogen source, but it did not promote PHB production like FP. A scheme for improved downstream extraction of PHB as well as the merits of using pleomorphic cells in the production of bioplastics is discussed.     

Effects of chronic sub-lethal oxidative stress on biofilm formation by Azotobacter vinelandii

This work showed that perturbations of the physiological steady-state level of reactive oxygen species (ROS) affected biofilm genesis and the characteristics of the model bacterium Azotobacter vinelandii. To get a continuous endogenous source of ROS, a strain exposed to chronic sub-lethal oxidative stress was deprived of the gene coding for the antioxidant rhodanese-like protein RhdA (MV474). In this study MV474 biofilm showed (i) a seven-fold higher growth rate, (ii) induction of catalase and alkyl-hydroxyl-peroxidase enzymes, (iii) higher average thicknesses due to increased production of a polysaccharide-rich extracellular matrix and (iv) less susceptibility to hydrogen peroxide than the wild-type strain (UW136). MV474 showed increased swimming and swarming activity and the swarming colonies experienced a higher level of oxidative stress compared to UW136. A continuous exogenous source of ROS increased biofilm formation in UW136. Overall, chronic sub-lethal oxidative events promoted sessile behavior in A. vinelandii.     

Nitrogen fixation in molybdenum-deficient continuous culture by a strain of Azotobacter vinelandii carrying a deletion of the structural genes for nitrogenase (nifHDK).

Steady-state chemostat cultures of Azotobacter vinelandii strain CA11, carrying a deletion of genes encoding the structural polypeptides of nitrogenase nifHDK, were established in a simple defined medium chemically purified to minimize contamination by Mo. The medium contained no utilizable N source. Growth was dependent on N2 (1.1 X 10(8) viable cells X ml-1 at D = 0.176 h-1), and was inhibited by Mo (20 nM). DNA hybridization showed the deletion to be stable during prolonged (55 days) growth in the chemostat (132 doublings). Since batch cultures, using unsupplemented 'spent' chemostat medium, showed good growth (1.9 X 10(8) cells X ml-1), no requirement for subnanomolar concentrations of Mo was found. The biomass yield, as the dilution rate (D) was varied, showed that the N content of the culture, protein and dry wt. increased as D was decreased, indicating that neither N2 nor O2 were limiting growth. The limiting nutrient was not identified. Substantial amounts of H2 were evolved by the chemostat cultures, probably as the result of inhibition of O2-dependent hydrogenase activity by nitrilotriacetic acid present in the medium. Over a range of D values approx. 50% of the electron flux through the alternative system was allocated to H+ reduction. C2H2 was a poor substrate, being reduced at 0.14-0.1 times the rate of N2 fixation, calculated from the N content of the cells. SO4(2-)-limited steady-state continuous cultures of strain UW136 (wild-type for nifHDK) had a 2-fold greater biomass in the presence of MoO4(2-) (1 microM). The significance of this finding for 'Mo-limited' continuous cultures [Eady & Robson (1984) Biochem. J. 224, 853-862] is discussed.     

固氮酶CrFe蛋白和MnFe蛋白的空间晶体生长

从分别牛长于含Mn和Cr培养基中的棕色固氮菌(Azotobacter vinelandii Lipmann)突变种UW3分离纯化出MnFe和CrFe蛋白。为适应包括固氮酶在内的氧敏感蛋白的空间晶体生长的要求,应用简易而适用的厌氧加样装置代替固氮酶实验室所用的笨重厌氧箱(dry box),在地面进行厌氧加样。在充满氮气的简便有机玻璃箱内厌氧加样的所有样品中,分别用液／液扩散法和汽相扩散的坐滴法都可在一周内使MnFe和CrFe蛋白在宇宙飞船上从溶液中结晶出来。在所用的数种蛋白沉淀剂中,飞船上形成的所有晶体都为单品,而地面上在多数沉淀剂中都生成大量挛晶。在相同沉淀剂中用液／液扩散法,飞船上生成CrFe蛋白的最大晶体比地面生成的最大晶体大1倍。而在相同沉淀剂中用汽相扩散的坐滴法,飞船上生成的MnFe蛋白最大晶体却没有地面生成的最大晶体大。这种差异也许是由不同结晶方法而不是不同蛋白所引起的。     

Process optimization for poly-beta-hydroxybutyrate production in a nitrogen fixing cyanobacterium, Nostoc muscorum using response surface methodology

A five-level-four-factor central composite rotary design was employed to find out the interactive effects of four variables, viz. concentrations of acetate, glucose and K2HPO4, and dark incubation period on poly-beta-hydroxybutyrate (PHB) production in a N2-fixing cyanobacterium, Nostoc muscorum. Acetate, glucose and dark incubation period exhibited positive impacts on PHB yield. Using response surface methodology (RSM), a second order polynomial equation was obtained by multiple regression analysis. A yield of 45.6% of dry cell weight (dcw) was achieved at reduced level of nutrients, i.e. 0.17% acetate, 0.16% glucose and 5 mg l(-1) K2HPO4 at a dark incubation period of 95 h as compared to 41.6% PHB yield in 0.4% acetate, 0.4% glucose and 40 mg l(-1) K2HPO4 at a dark incubation period of 168 h under single factor optimization strategy.     

Transformation of Azotobacter vinelandii OP with a broad host range plasmid containing a cloned chromosomal nif-DNA marker

The non-nitrogen-fixing (Nif-) strain UW10 of Azotobacter vinelandii OP (UW) was naturally induced to competence and transformed with broad host range plasmid pKT210 containing the cloned wild-type nif-10 locus from A. vinelandii UW (Nif+); this marker was unable to complement the nif-10 mutation in trans, but could through recombination with the chromosome. The most frequent type of transformation event observed was recombination between the homologous regions of the plasmid and chromosome (producing Nif+ transformants) with loss of the plasmid vector. At a substantially lower frequency, transformants expressing the plasmid-encoded antibiotic resistance determinants were isolated which were phenotypically Nif-. Agarose gel electrophoresis showed that these transformants contained a plasmid migrating with the same mobility as the original donor plasmid. During culture these transformants acquired a Nif+ phenotype without the loss of the plasmid, as judged by the use of a hybridization probe specific for the cloned nif-DNA fragment. These data indicate that plasmids carrying sequences homologous to chromosomal sequences could be maintained in recombination-proficient A. vinelandii UW. The introduction of plasmids containing sequences homologous to chromosomal sequences was facilitated by prelinearization of the plasmid using a restriction endonuclease generating cohesive ends. Because the site of linearization could be chosen outside the region of shared homology, it was unlikely that the route of plasmid establishment occurred via a homology-facilitated transformation mechanism. The data also indicated that A. vinelandii UW could harbor broad host range cloning vectors based on plasmid RSF1010 without significant impairment of its nitrogen-fixation ability.     

Strategies for adaptation to antibiotics in wild type <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> and in the strains with small colony phenotype

Emergence of ciprofloxacin stress-induced mutants in the cultures of a collection strain Pseudomonas aeruginosa ATCC 27853 and of two strains with a small colony phenotype, which were isolated from a swimming pool biofilm, was studied. In biofilm cultures of the small colony phenotype strains, which were already resistant to hypochlorite, prolonged incubation (up to 16 days) with sublethal ciprofloxacin concentrations was shown to result in emergence of the cells, which are resistant to the antibiotic and form colonies on media with rifampicin (100 μg/mL) and streptomycin (50 μg/mL). Under the same conditions, the mechanisms of temporary adaptation are switched on in the cells of strain ATCC 27853, which enabled its shortterm survival at an average level in liquid media and provided for colony formation on solid medium with ciprofloxacin (0.2 μg/mL). Only 20% of these colonies remained viable when transferred to a higher antibiotic concentration (2 μg/mL).     

The shxVW locus is essential for oxidation of inorganic sulfur and molecular hydrogen by Paracoccus pantotrophus GB17: a novel function for lithotrophy

CydR is an Fnr-like protein in the obligatory aerobic nitrogen-fixing bacterium Azotobacter vinelandii. The cydR mutant overproduces the cytochrome bd terminal oxidase. Using two-dimensional polyacrylamide gel electrophoresis, we showed that beta-ketothiolase and acetoacetyl-CoA reductase were also overexpressed in the cydR mutant. Fumarase C and a coenzyme A transferase, possibly succinyl-SCoA transferase, were decreased in this mutant. Enzyme assays confirmed the elevated beta-ketothiolase and acetoacetyl-CoA reductase activities in this mutant. The cydR mutant accumulated poly-beta-hydroxybutyrate throughout the exponential growth phase, unlike the wild-type strain that only accumulated poly-beta-hydroxybutyrate during stationary phase. The results demonstrate that CydR controls poly-beta-hydroxybutyrate synthesis in A. vinelandii.     

Carbohydrate and Amino Acid Fermentation in the Free-Living Primitive Protozoon Hexamita sp

Hexamita sp. is an amitochondriate free-living diplomonad which inhabits O(2)-limited environments, such as the deep waters and sediments of lakes and marine basins. C nuclear magnetic resonance spectroscopy reveals ethanol, lactate, acetate, and alanine as products of glucose fermentation under microaerobic conditions (23 to 34 muM O(2)). Propionic acid and butyric acid were also detected and are believed to be the result of fermentation of alternative substrates. Production of organic acids was greatest under microaerobic conditions (15 muM O(2)) and decreased under anaerobic (<0.25 muM O(2)) and aerobic (200 to 250 muM O(2)) conditions. Microaerobic incubation resulted in the production of high levels of oxidized end products (70% acetate) compared to that produced under anoxic conditions (20% acetate). In addition, data suggest that Hexamita cells contain the arginine dihydrolase pathway, generating energy from the catabolism of arginine to citrulline, ornithine, NH(4), and CO(2). The rate of arginine catabolism was higher under anoxic conditions than under microaerobic conditions. Hexamita cells were able to grow in the absence of a carbohydrate source, albeit with a lower growth rate and yield.     

Physiological regulation and optimization of lipase activity in Pseudomonas aeruginosa EF2.

Physiological regulation of extracellular lipase activity by a newly-isolated, thermotolerant strain of Pseudomonas aeruginosa (strain EF2) was investigated by growing the organism under various conditions in batch, fed-batch and continuous culture. Lipase activity, measured as the rate of olive oil (predominantly triolein) hydrolysis, was weakly induced by general carbon and/or energy limitation, strongly induced by a wide range of fatty acyl esters including triglycerides, Spans and Tweens, and repressed by long-chain fatty acids including oleic acid. The highest lipase activities were observed during the stationary phase of batch cultures grown on Tween 80, and with Tween 80-limited fed-batch and continuous cultures grown at low specific growth rates. The lipase activity of Tween 80-limited continuous cultures was optimized with respect to pH and temperature using response surface analysis; maximum activity occurred during growth at pH 6.5, 35.5 degrees C, at a dilution rate of 0.04 h-1. Under these conditions the culture exhibited a lipase activity of 39 LU (mg cells)-1 and a specific rate of lipase production (qLipase) of 1.56 LU (mg cells)-1 h-1 (1 LU equalled 1 mumol fatty acid released min-1). Esterase activity, measured with p-nitrophenyl acetate as substrate, varied approximately in parallel with lipase activity under all growth conditions, suggesting that a single enzyme may catalyse both activities.     

Production of poly-β-hydroxybutyrate by Azotobacter vinelandii strain UWD during growth on molasses and other complex carbon sources

Summary Azotobacter vinelandii strain UWD formed >2 mg/ml poly--hydroxybutyrate (pHB) during exponential growth in media containing ammonium acetate and 1% w/v glucose, fructose, sucrose, or maltose, and >1.5 mg/ml with 1% w/v sodium gluconate or glycerol. After acetate exhaustion, pHB formation accompanied carbohydrate utilization and pHB rapidly accounted for 53%–70% of the cell mass. Strain UWD also formed >2 mg/ml pHB when it was grown with 2% w/v corn syrup, cane molasses, beet molasses, or malt extract. Beet molasses had a growth stimulatory effect which promoted higher yields of pHB/ml and a high ratio of pHB/protein. Malt extract also promoted higher yields of pHB/ml. In this case, pHB formation was no longer subject to acetate repression and the cells contained a higher ratio of pHB/protein. This study shows that unrefined carbon sources support pHB formation in strain UWD and that the yields of pHB were comparable to or better than those obtained with refined carbon sources.     

Role of the Azotobacter vinelandii nitrogenase-protective shethna protein in preventing oxygen-mediated cell death

Azotobacter vinelandii strains lacking the nitrogenase-protective Shethna protein lost viability upon carbon-substrate deprivation in the presence of oxygen. This viability loss was dependent upon the N(2)-fixing status of cultures (N(2)-fixing cells lost viability, while non-N(2)-fixing cells did not) and on the ambient O(2) level. Supra-atmosheric O(2) tensions (40% partial pressure) decreased the viable cell number of the mutant further, and the mutant had a slightly higher spontaneous mutation frequency than the wild type in the high-O(2) conditions. Iron starvation conditions, which resulted in fourfold-reduced superoxide dismutase levels, were also highly detrimental to the viability of the protective protein mutants, but these conditions did not affect the viability of the wild-type strain. Nitrogenase or other powerful reductants associated with N(2) fixation may be sources of damaging partially reduced oxygen species, and the production of such species are perhaps minimized by the Shethna protein.     

Growth and exopolysaccharide production by Azotobacter vinelandii in media containing phenolic acids

Azotobacter vinelandii was cultured in chemically defined, nitrogen-free media supplemented with either 4-hydroxyphenylacetic, 4-hydroxybenzoic or protocatechuic acids at different concentrations. Under these conditions, biomass, exopolysaccharide production and consumption of the carbon sources were investigated. Results obtained throughout this study showed that 4-hydroxyphenylacetic acid yielded the highest growth levels measured as biomass, and exopolysaccharide production, independently of the concentration of the carbon source tested. 4-Hydroxybenzoic acid also supported appreciable growth and exopolysaccharide recovery by A. vinelandii. Protocatechuic acid, however, only allowed a very small production of biomass and exopolysaccharide by the strain investigated. Under given conditions, more than 26% of the carbon source supplied was converted to exopolysaccharide in cultures of A. vinelandii .     

Measurement of autolysis in submerged batch cultures of Penicillium chrysogenum

The process of cellular autolysis was studied in an industrial strain of Penicillium chrysogenum by a range of methods, including assessment of biomass decline, NH+4 release, changes in culture apparent viscosity, and by means of a quantitative assessment of changes in micromorphology using a computerized image analysis system. The pattern of total intracellular proteolytic and beta-1, 3-glucanolytic activity in the culture was also examined. The overall aim was to identify a suitable method, or methods, for examining the extent of autolysis in fungal cultures. Autolysis was studied in submerged batch processes, where DOT was maintained above 40% saturation (non-O2-limited), and, under O2-limited conditions. Both N and O2 limitation promoted extensive culture autolysis. Image analysis techniques were perhaps the most sensitive method of assessing the progress of autolysis in the culture. Autolytic regions within some hyphae were apparent even during growth phase, but became much more widespread as the process proceeded. The early stages of autolysis involved continued energy source consumption, increased carbon dioxide evolution rate, degradation of penicillin, and decreased broth filterability. Later stages involved widespread mycelial fragmentation, with some regrowth (cryptic growth) occurring in non-O2-limited cultures. Intracellular proteolytic activity showed two peaks, one during the growth phase, and the other during autolysis. Autolysis was also associated with a distinct peak in beta-1,3-glucanolytic activity, indicating that degradation of cell wall matrix polymers may be occurring during autolysis in this strain of P. chrysogenum.