Influence of glucose on glycerol metabolism by wild-type and mutant strains of Clostridium butyricum E5 grown in chemostat culture

In order to improve the yield of 1,3-propanediol (1,3-PPD) in Clostridium butyricum E5, we carried out cofermentation experiments on glucose/glycerol mixtures in chemostat culture. The results showed the influence of the ratio of the two carbon substrates on the production of the required diol. The progressive increase of glucose in culture medium containing a given concentration of glycerol made it possible to highlight the deviation of carbon flow from the oxidative towards the reducing pathway, in order to maintain the oxidation/reduction balance in the cell. The conversion of glycerol into 1,3-PPD thus increased from 0.63 mol mol(-1), without the addition of glucose, to a maximum of 0.89 mol mol(-1) for a molar glucose/glycerol ratio of 0.2 for the wild-type strain. The same experiments carried out with the mutant MD strain, which is resistant to allyl alcohol, led to similar results but with a maximum of 0.84 mol mol(-1) for a glucose/glycerol molar ratio of 0.1. Beyond a molar ratio of 0.2, the biosynthesis of enzymes for the glycerol metabolism was less subject to catabolic repression by glucose in the mutant MD strain than in the wild-type strain.     

一株1,3-丙二醇生产菌的分离鉴定及其发酵特性

从活性污泥中分离筛选得到一株能代谢甘油生产1,3-丙二醇(1,3-PD)的菌株2-1,通过形态学鉴定、生理生化试验、16S rRNA序列分析对菌株分类学地位进行鉴定,用MEGA 4.1软件构建的系统发育树显示菌株2-1与Klebsiella pneumoniae(CP001891)的亲缘关系最近。16S rDNA序列同源性比较发现,菌株2-1与模式菌株同源率为95.4%,疑似为新种。对菌株2-1在5 L发酵罐中进行发酵特性研究,分批补料发酵时得到较高的1,3-PD终浓度,达到63.5 g/L,此时生产强度为2.19 g/(L.h),底物转化率0.64 mol/mol。     

Eliminating side products and increasing succinate yields in engineered strains of Escherichia coli C

Derivatives of Escherichia coli C were previously described for succinate production by combining the deletion of genes that disrupt fermentation pathways for alternative products (ldhA::FRT, adhE::FRT, ackA::FRT, focA-pflB::FRT, mgsA, poxB) with growth-based selection for increased ATP production. The resulting strain, KJ073, produced 1.2 mol of succinate per mol glucose in mineral salts medium with acetate, malate, and pyruvate as significant co-products. KJ073 has been further improved by removing residual recombinase sites (FRT sites) from the chromosomal regions of gene deletion to create a strain devoid of foreign DNA, strain KJ091(DeltaldhA DeltaadhE DeltaackA DeltafocA-pflB DeltamgsA DeltapoxB). KJ091 was further engineered for improvements in succinate production. Deletion of the threonine decarboxylase (tdcD; acetate kinase homologue) and 2-ketobutyrate formate-lyase (tdcE; pyruvate formate-lyase homologue) reduced the acetate level by 50% and increased succinate yield (1.3 mol mol(-1) glucose) by almost 10% as compared to KJ091 and KJ073. Deletion of two genes involved in oxaloacetate metabolism, aspartate aminotransferase (aspC) and the NAD(+)-linked malic enzyme (sfcA) (KJ122) significantly increased succinate yield (1.5 mol mol(-1) glucose), succinate titer (700 mM), and average volumetric productivity (0.9 g L(-1) h(-1)). Residual pyruvate and acetate were substantially reduced by further deletion of pta encoding phosphotransacetylase to produce KJ134 (DeltaldhA DeltaadhE DeltafocA-pflB DeltamgsA DeltapoxB DeltatdcDE DeltacitF DeltaaspC DeltasfcA Deltapta-ackA). Strains KJ122 and KJ134 produced near theoretical yields of succinate during simple, anaerobic, batch fermentations using mineral salts medium. Both may be useful as biocatalysts for the commercial production of succinate.     

Effects of light on the microcystin content of Microcystis strain PCC 7806

Many cyanobacteria produce microcystins, hepatotoxic cyclic heptapeptides that can affect animals and humans. The effects of photosynthetically active radiation (PAR) on microcystin production by Microcystis strain PCC 7806 were studied in continuous cultures. Microcystis strain PCC 7806 was grown under PAR intensities between 10 and 403 micro mol of photons m(-2) s(-1) on a light-dark rhythm of 12 h -12 h. The microcystin concentration per cell, per unit biovolume and protein, was estimated under steady-state and transient-state conditions and on a diurnal timescale. The cellular microcystin content varied between 34.5 and 81.4 fg cell(-1) and was significantly positively correlated with growth rate under PAR-limited growth but not under PAR-saturated growth. Microcystin production and PAR showed a significant positive correlation under PAR-limited growth and a significant negative correlation under PAR-saturated growth. The microcystin concentration, as a ratio with respect to biovolume and protein, correlated neither with growth rate nor with PAR. Adaptation of microcystin production to a higher irradiance during transient states lasted for 5 days. During the period of illumination at a PAR of 10 and 40 micro mol of photons m(-2) s(-1), the intracellular microcystin content increased to values 10 to 20% higher than those at the end of the dark period. Extracellular (dissolved) microcystin concentrations were 20 times higher at 40 micro mol of photons m(-2) s(-1) than at 10 micro mol of photons m(-2) s(-1) and did not change significantly during the light-dark cycles at both irradiances. In summary, our results showed a positive effect of PAR on microcystin production and content of Microcystis strain PCC 7806 up to the point where the maximum growth rate is reached, while at higher irradiances the microcystin production is inhibited.     

Formation of hydride-Meisenheimer complexes of picric acid (2,4, 6-trinitrophenol) and 2,4-dinitrophenol during mineralization of picric acid by Nocardioides sp. strain CB 22-2

There are only a few examples of microbial conversion of picric acid (2,4,6-trinitrophenol). None of the organisms that have been described previously is able to use this compound as a sole source of carbon, nitrogen, and energy at high rates. In this study we isolated and characterized a strain, strain CB 22-2, that was able to use picric acid as a sole source of carbon and energy at concentrations up to 40 mM and at rates of 1.6 mmol. h(-1). g (dry weight) of cells(-1) in continuous cultures and 920 micromol. h(-1). g (dry weight) of cells(-1) in flasks. In addition, this strain was able to use picric acid as a sole source of nitrogen at comparable rates in a nitrogen-free medium. Biochemical characterization and 16S ribosomal DNA analysis revealed that strain CB 22-2 is a Nocardioides sp. strain. High-pressure liquid chromatography and UV-visible light data, the low residual chemical oxygen demand, and the stoichiometric release of 2.9 +/- 0.1 mol of nitrite per mol of picric acid provided strong evidence that complete mineralization of picric acid occurred. During transformation, the metabolites detected in the culture supernatant were the [H-]-Meisenheimer complexes of picric acid and 2,4-dinitrophenol (H--DNP), as well as 2,4-dinitrophenol. Experiments performed with crude extracts revealed that H--DNP formation indeed is a physiologically relevant step in picric acid metabolism.     

Characterization of the corrinoid iron-sulfur protein tetrachloroethene reductive dehalogenase of Dehalobacter restrictus

The membrane-bound tetrachloroethene reductive dehalogenase (PCE-RDase) (PceA; EC 1.97.1.8), the terminal component of the respiratory chain of Dehalobacter restrictus, was purified 25-fold to apparent electrophoretic homogeneity. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis revealed a single band with an apparent molecular mass of 60 +/- 1 kDa, whereas the native molecular mass was 71 +/- 8 kDa according to size exclusion chromatography in the presence of the detergent octyl-beta-D-glucopyranoside. The monomeric enzyme contained (per mol of the 60-kDa subunit) 1.0 +/- 0.1 mol of cobalamin, 0.6 +/- 0.02 mol of cobalt, 7.1 +/- 0.6 mol of iron, and 5.8 +/- 0.5 mol of acid-labile sulfur. Purified PceA catalyzed the reductive dechlorination of tetrachloroethene and trichloroethene to cis-1,2-dichloroethene with a specific activity of 250 +/- 12 nkat/mg of protein. In addition, several chloroethanes and tetrachloromethane caused methyl viologen oxidation in the presence of PceA. The K(m) values for tetrachloroethene, trichloroethene, and methyl viologen were 20.4 +/- 3.2, 23.7 +/- 5.2, and 47 +/- 10 micro M, respectively. The PceA exhibited the highest activity at pH 8.1 and was oxygen sensitive, with a half-life of activity of 280 min upon exposure to air. Based on the almost identical N-terminal amino acid sequences of PceA of Dehalobacter restrictus, Desulfitobacterium hafniense strain TCE1 (formerly Desulfitobacterium frappieri strain TCE1), and Desulfitobacterium hafniense strain PCE-S (formerly Desulfitobacterium frappieri strain PCE-S), the pceA genes of the first two organisms were cloned and sequenced. Together with the pceA genes of Desulfitobacterium hafniense strains PCE-S and Y51, the pceA genes of Desulfitobacterium hafniense strain TCE1 and Dehalobacter restrictus form a coherent group of reductive dehalogenases with almost 100% sequence identity. Also, the pceB genes, which may code for a membrane anchor protein of PceA, and the intergenic regions of Dehalobacter restrictus and the three desulfitobacteria had identical sequences. Whereas the cprB (chlorophenol reductive dehalogenase) genes of chlorophenol-dehalorespiring bacteria are always located upstream of cprA, all pceB genes known so far are located downstream of pceA. The possible consequences of this feature for the annotation of putative reductive dehalogenase genes are discussed, as are the sequence around the iron-sulfur cluster binding motifs and the type of iron-sulfur clusters of the reductive dehalogenases of Dehalobacter restrictus and Desulfitobacterium dehalogenans identified by electron paramagnetic resonance spectroscopy.     

L-malate production by metabolically engineered Escherichia coli

Escherichia coli strains (KJ060 and KJ073) that were previously developed for succinate production have now been modified for malate production. Many unexpected changes were observed during this investigation. The initial strategy of deleting fumarase isoenzymes was ineffective, and succinate continued to accumulate. Surprisingly, a mutation in fumarate reductase alone was sufficient to redirect carbon flow into malate even in the presence of fumarase. Further deletions were needed to inactivate malic enzymes (typically gluconeogenic) and prevent conversion to pyruvate. However, deletion of these genes (sfcA and maeB) resulted in the unexpected accumulation of D-lactate despite the prior deletion of mgsA and ldhA and the absence of apparent lactate dehydrogenase activity. Although the metabolic source of this D-lactate was not identified, lactate accumulation was increased by supplementation with pyruvate and decreased by the deletion of either pyruvate kinase gene (pykA or pykF) to reduce the supply of pyruvate. Many of the gene deletions adversely affected growth and cell yield in minimal medium under anaerobic conditions, and volumetric rates of malate production remained low. The final strain (XZ658) produced 163 mM malate, with a yield of 1.0 mol (mol glucose(-1)), half of the theoretical maximum. Using a two-stage process (aerobic cell growth and anaerobic malate production), this engineered strain produced 253 mM malate (34 g liter(-1)) within 72 h, with a higher yield (1.42 mol mol(-1)) and productivity (0.47 g liter(-1) h(-1)). This malate yield and productivity are equal to or better than those of other known biocatalysts.     

Production of xylitol from D-xylose by recombinant Lactococcus lactis

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

灵芝原生质体制备、再生及融合的研究

报道不同菌龄、酶液浓度、稳渗剂对灵芝原生质体产率及不同种类、不同浓度的稳渗剂对原生质体再生的影响。结果表明,诱变后具抗药性标记的“中国红灵芝”菌种（mH1）原生质体制备时菌丝最适菌龄为48小时,酶液浓度为3％,稳渗剂以0．6mol／L蔗糖为佳;诱变后具抗药性标记的“韩国红灵芝”（mK1）原生质体制备时菌丝最适菌龄为40小时,酶液浓度为1％,稳渗剂为0.4mol／L甘露醇时原生质体产率最高。mH1,mK1原生质体均以蔗糖作稳渗剂再生率较高,其最佳浓度为0．6mol／L。在该条件下mH1原生质体再生率为3．20×10-2,mK1为5．40×10-2。在此基础上,以30％的PEG作为融合诱导剂进行灵芝原生质体融合,并获得了融合子,融合率为140×10-2。     

Process strategies to enhance pyruvate production with recombinant Escherichia coli: from repetitive fed-batch to in situ product recovery with fully integrated electrodialysis

Using the pyruvate production strain Escherichia coli YYC202 ldhA::Kan different process alternatives are studied with the aim of preventing potential product inhibition by appropriate product separation. This strain is completely blocked in its ability to convert pyruvate into acetyl-CoA or acetate, resulting in acetate auxotrophy during growth in glucose minimal medium. Continuous experiments with cell retention, repetitive fed-batch, and an in situ product recovery (ISPR) process with fully integrated electrodialysis were tested. Although the continuous approach achieved a high volumetric productivity (QP) of 110 g L(-1) d(-1), this approach was not pursued because of long-term production strain instabilities. The highest pyruvate/glucose molar yield of up to 1.78 mol mol(-1) together with high QP 145 g L(-1) d(-1) and high pyruvate titers was achieved by the repetitive fed-batch approach. To separate pyruvate from fermentation broth a fully integrated continuous process was developed. In this process electrodialysis was used as a separation unit. Under optimum conditions a (calculated) final pyruvate titer of >900 mmol L(-1) (79 g L(-1)) was achieved.     

Acetate threshold concentrations suggest varying energy requirements during anaerobic respiration by Anaeromyxobacter dehalogenans

Acetate threshold concentrations were determined under chlororespiring and Fe(III)-reducing conditions for Anaeromyxobacter dehalogenans strain 2CP-C. The acetate threshold concentrations measured were 69 +/- 4, 19 +/- 8, and <1 nM for chlororespiration, amorphous Fe(III) reduction, and Fe(III) citrate reduction, respectively. Residual DeltaG values of -75.4 kJ/mol of electrons for chlororespiration and -41.5 kJ/mol of electrons for amorphous Fe(III) reduction were calculated at the acetate threshold concentration. By comparing threshold concentrations for different metabolisms in a single organism, this study provides insight into the metabolic use of energy under different growth conditions.     

Malic acid production by Saccharomyces cerevisiae: engineering of pyruvate carboxylation, oxaloacetate reduction, and malate export

Malic acid is a potential biomass-derivable "building block" for chemical synthesis. Since wild-type Saccharomyces cerevisiae strains produce only low levels of malate, metabolic engineering is required to achieve efficient malate production with this yeast. A promising pathway for malate production from glucose proceeds via carboxylation of pyruvate, followed by reduction of oxaloacetate to malate. This redox- and ATP-neutral, CO(2)-fixing pathway has a theoretical maximum yield of 2 mol malate (mol glucose)(-1). A previously engineered glucose-tolerant, C(2)-independent pyruvate decarboxylase-negative S. cerevisiae strain was used as the platform to evaluate the impact of individual and combined introduction of three genetic modifications: (i) overexpression of the native pyruvate carboxylase encoded by PYC2, (ii) high-level expression of an allele of the MDH3 gene, of which the encoded malate dehydrogenase was retargeted to the cytosol by deletion of the C-terminal peroxisomal targeting sequence, and (iii) functional expression of the Schizosaccharomyces pombe malate transporter gene SpMAE1. While single or double modifications improved malate production, the highest malate yields and titers were obtained with the simultaneous introduction of all three modifications. In glucose-grown batch cultures, the resulting engineered strain produced malate at titers of up to 59 g liter(-1) at a malate yield of 0.42 mol (mol glucose)(-1). Metabolic flux analysis showed that metabolite labeling patterns observed upon nuclear magnetic resonance analyses of cultures grown on (13)C-labeled glucose were consistent with the envisaged nonoxidative, fermentative pathway for malate production. The engineered strains still produced substantial amounts of pyruvate, indicating that the pathway efficiency can be further improved.     

Inactivation of aldehyde dehydrogenase: a key factor for engineering 1,3-propanediol production by Klebsiella pneumoniae

Production of 1,3-propanediol (1,3-PD) from glycerol by Klebsiella pneumoniae is restrained by ethanol formation. The first step in the formation of ethanol from acetyl-CoA is catalyzed by aldehyde dehydrogenase (ALDH), an enzyme that competes with 1,3-PD oxidoreductase for the cofactor NADH. This study aimed to improve the production of 1,3-PD by engineering the ethanol formation pathway. An inactivation mutation of the aldA gene encoding ALDH in K. pneumoniae YMU2 was generated by insertion of a tetracycline resistance marker. Inactivation of ALDH resulted in a nearly abolished ethanol formation but a significantly improved 1,3-PD production. Metabolic flux analysis revealed that a pronounced redistribution of intracellular metabolic flux occurred. The final titer, the productivity of 1,3-PD and the yield of 1,3-PD relative to glycerol of the mutant strain reached 927.6 mmol L(-1), 14.05 mmol L(-1)h(-1) and 0.699 mol mol(-1), respectively, which were much higher than those of the parent strain. In addition, the specific 1,3-PD-producing capability (1,3-PD produced per gram of cells) of the mutant strain was 2-fold that of the parent strain due to a lower growth yield of the mutant. By increasing NADH availability, this study demonstrates an important metabolic engineering approach to improve the efficiency of oxidoreduction-coupled bioprocesses.     

Ring cleavage and degradative pathway of cyanuric acid in bacteria.

The degradative pathway of cyanuric acid [1,3,5-triazine-2,4,6(1H,3H,5H)-trione] was examined in Pseudomonas sp. strain D. The bacterium grew with cyanuric acid, biuret, urea or NH4+ as sole source of nitrogen, and each substrate was entirely metabolized concomitantly with growth. Enzymes from strain D were separated by chromatography on DEAE-cellulose and three reactions were examined. Cyanuric acid (1 mol) was converted stoichiometrically into 1.0 mol of CO2 and 1.1 mol of biuret, which was conclusively identified. Biuret (1 mol) was converted stoichiometrically into 1.1 mol of NH4+, about 1 mol of CO2 and 1.0 mol of urea, which was conclusively identified. Urea (1 mol) was converted into 1.9 mol of NH4+ and 1.0 mol of CO2. The reactions proceeded under aerobic or anoxic conditions and were presumed to be hydrolytic. Data indicate that the same pathway occurred in another pseudomonad and a strain of Klebsiella pneumoniae.     

Increase in Silk Production by the Silkworm,Bombyx morì L., due to Oral Administration of a Juvenile Hormone Analog

(R)-1,3-butanediol ((R)-1,3-BD) is an important substrate for the synthesis of industrial chemicals. Despite its large demand, a bioprocess for the efficient production of 1,3-BD from renewable resources has not been developed. We previously reported the construction of recombinant Escherichia coli that could efficiently produce (R)-1,3-BD from glucose. In this study, the fermentation conditions were optimized to further improve 1,3-BD production by the recombinant strain. A batch fermentation was performed with an optimized overall oxygen transfer coefficient (82.3?h^?1) and pH (5.5); the 1,3-BD concentration reached 98.5?mM after 36?h with high-yield (0.444?mol (mol glucose)^?1) and a high maximum production rate (3.63?mM?h^?1). In addition, a fed-batch fermentation enabled the recombinant strain to produce 174.8?mM 1,3-BD after 96?h cultivation with a yield of 0.372?mol (mol glucose)^?1, a maximum production rate of 3.90?mM?h^?1, and a 98.6% enantiomeric excess (% ee) of (R)-1,3-BD.     

Pyruvate formation and suppression in recombinant Bacillus megaterium cultivation

A recombinant Bacillus megaterium strain showed the ability to secrete large amounts of pyruvate (up to 27.8 gl( -1)) for growth rates larger than 0.15 h(-1). Cultivation below this growth rate avoids pyruvate formation while minimizing acetate and succinate production. Using exponential feeding, final biomass concentrations of up to 80 g l(-1) were achieved. Overall molar yields for the experiments with pyruvate formation were as high as 0.79 mol mol(-1). Pyruvate formation was caused by the discrepancy between glycolytic and pyruvate dehydrogenase reaction/tricarboxylic acid cycle capacities during glucose excess. High pyruvate resulted in deceleration and subsequent cessation of growth. In addition, this inhibitory effect is likely associated with the phoshoenolpyruvate:glucose phosphotransferase system used by B. megaterium as the main importer for glucose.     

The Effect of Cadmium on Tobacco Cell Culture and the Selection of Potentially Cd-Resistant Cell lines

The effect of different concentrations of cadmium on the viability, cell division, and the total increase in the biomass of the VBI-O cell strain of tobacco (Nicotiana tabacumL., Virginia Bright Italia) was followed. The concentration of 10^-6 mol 1^-1 Cd²⁺ was fully tolerated by this strain, a nearly total inhibition of cell division and high cell mortality rate ocsicurred at the concentration of 10^-4 mol1{si-1} Cd²⁺. Following a long-term exposure of the culture to gradually increasing cadmium concentrations, seven cell lines able to grow on media containing 10^-4 mol 1^-1 Cd²⁺ were derived. Phenotype diversity of the isolated cell lines likely causes of the disappearance of the resistance character are discussed.     

Physiological and genetic engineering of cytosolic redox metabolism in Saccharomyces cerevisiae for improved glycerol production

Previous metabolic engineering strategies for improving glycerol production by Saccharomyces cerevisiae were constrained to a maximum theoretical glycerol yield of 1 mol.(molglucose)(-1) due to the introduction of rigid carbon, ATP or redox stoichiometries. In the present study, we sought to circumvent these constraints by (i) maintaining flexibility at fructose-1,6-bisphosphatase and triosephosphate isomerase, while (ii) eliminating reactions that compete with glycerol formation for cytosolic NADH and (iii) enabling oxidative catabolism within the mitochondrial matrix. In aerobic, glucose-grown batch cultures a S. cerevisiae strain, in which the pyruvate decarboxylases the external NADH dehydrogenases and the respiratory chain-linked glycerol-3-phosphate dehydrogenase were deleted for this purpose, produced glycerol at a yield of 0.90 mol.(molglucose)(-1). In aerobic glucose-limited chemostat cultures, the glycerol yield was ca. 25% lower, suggesting the involvement of an alternative glucose-sensitive mechanism for oxidation of cytosolic NADH. Nevertheless, in vivo generation of additional cytosolic NADH by co-feeding of formate to aerobic, glucose-limited chemostat cultures increased the glycerol yield on glucose to 1.08 mol mol(-1). To our knowledge, this is the highest glycerol yield reported for S. cerevisiae.     

Comparison of high pressure-induced dissociation of single-stranded DNA-binding protein (SSB) from high pressure-sensitive and high pressure-adapted marine Shewanella species

The effects of hydrostatic pressure on protein quaternary structure were compared for recombinant single-stranded DNA-binding protein (SSB) derived from piezosensitive, piezotolerant, and obligately piezophilic ("pressure-loving") marine Shewanella strains. The pressure-induced dissociation of the oligomeric SSB proteins was investigated using fluorescence anisotropy. The SSBs all exhibited striking similarity in the pressure-dependent behavior of the fluorescence intensity and emission spectrum as well as in their dissociation constants at atmospheric pressure. The free energies of subunit association into tetramers for all SSBs were between -27 and -30 kcal mol(-1). However, SSB from the piezosensitive Shewanella strain S. hanedai was more sensitive to pressure than that of the SSB proteins from the piezotolerant or piezophilic bacteria. The volume change of association obtained from the pressure dependence of dissociation at a fixed protein concentration (Delta V(p)) for SSB from S. hanedai was 394-402 ml mol(-1). The Delta V(p) values for SSB from the deeper-living Shewanellas were smaller and ranged from 253 to 307 ml mol(-1). Differences between the primary structures of the SSB proteins that could correlate with differences in sensitivity to pressure-induced dissociation were examined.