Analysis of the proteome of Pseudomonas putida KT2440 grown on different sources of carbon and energy

Using 2D electrophoresis the protein expression pattern during growth on carbon sources with different impact on carbon catabolite repression of phenol degradation was analysed in a derivative of Pseudomonas putida KT2440. The cytosolic protein pattern of cells growing on phenol or the non-repressive substrate pyruvate was almost identical, but showed significant differences to that of cells growing with the repressive substrates succinate or glucose. Proteins, which were mainly expressed in the presence of phenol or pyruvate, could be assigned to the functional groups of transport, detoxification, stress response, amino acid, energy, carbohydrate and nucleotide metabolism. The addition of succinate to cells growing with phenol ('shift-up') resulted in the inhibition of the synthesis of these proteins. Proteins with enhanced expression at growth with succinate or glucose were proteins for de novo synthesis of nucleotides, amino acids and enzymes of the TCA cycle. The synthesis of proteins, necessary for phenol catabolism was regulated in different manners following the addition of succinate. Whereas the synthesis of Phl-proteins (subunits of the phenolhydroxylase) only decreased slowly, was the translation of the Cat-proteins (catechol 1,2-dioxygenase, cis,cis-muconate cycloisomerase and muconolactone isomerase) repressed immediately and the synthesis of the Pca-proteins (beta-ketoadipate enolactone hydrolase, beta-ketoadipate succinyl-CoA transferase and beta-ketoadipyl CoA thiolase) remained unaffected.     

Chemostat-based proteomic analysis of toluene-affected Pseudomonas putida S12

The aim of this study was to assess the cellular response of the solvent-tolerant Pseudomonas putida S12 to toluene as the single effector. Proteomic analysis (two-dimensional difference-in-gel-electrophoresis) was used to assess the response of P. putida S12 cultured in chemostats. This approach ensures constant growth conditions, both in the presence and absence of toluene. A considerable negative effect of toluene on the cell yield was found. The need for energy in the defence against toluene was reflected by differentially expressed proteins for cell energy management. In toluene-stressed cells the balance between proton motive force (PMF) enforcing and dissipating systems was shifted. NAD(P)H generating systems were upregulated whereas the major proton-driven system, ATP synthase, was downregulated. Other differentially expressed proteins were identified: outer membrane proteins, transport proteins, stress-related proteins and translation-related proteins. In addition, a protein with no assigned function was found. This study yielded a more detailed view of the effect of toluene on the intracellular energy management of P. putida S12 and several novel leads have been obtained for further targeted investigations.     

Effect of Organic Solvents on the Yield of Solvent-Tolerant Pseudomonas putida S12

Solvent-tolerant microorganisms are useful in biotransformations with whole cells in two-phase solvent-water systems. The results presented here describe the effects that organic solvents have on the growth of these organisms. The maximal growth rate of Pseudomonas putida S12, 0.8 h⁻¹, was not affected by toluene in batch cultures, but in chemostat cultures the solvent decreased the maximal growth rate by nearly 50%. Toluene, ethylbenzene, propylbenzene, xylene, hexane, and cyclohexane reduced the biomass yield, and this effect depended on the concentration of the solvent in the bacterial membrane and not on its chemical structure. The dose response to solvents in terms of yield was linear up to an approximately 200 mM concentration of solvent in the bacterial membrane, both in the wild type and in a mutant lacking an active efflux system for toluene. Above this critical concentration the yield of the wild type remained constant at 0.2 g of protein/g of glucose with increasing concentrations of toluene. The reduction of the yield in the presence of solvents is due to a maintenance higher by a factor of three or four as well as to a decrease of the maximum growth yield by 33%. Therefore, energy-consuming adaptation processes as well as the uncoupling effect of the solvents reduce the yield of the tolerant cells.     

Establishment of Oxidative d-Xylose Metabolism in Pseudomonas putida S12

The oxidative d-xylose catabolic pathway of Caulobacter crescentus, encoded by the xylXABCD operon, was expressed in the gram-negative bacterium Pseudomonas putida S12. This engineered transformant strain was able to grow on d-xylose as a sole carbon source with a biomass yield of 53% (based on g [dry weight] g d-xylose⁻¹) and a maximum growth rate of 0.21 h⁻¹. Remarkably, most of the genes of the xylXABCD operon appeared to be dispensable for growth on d-xylose. Only the xylD gene, encoding d-xylonate dehydratase, proved to be essential for establishing an oxidative d-xylose catabolic pathway in P. putida S12. The growth performance on d-xylose was, however, greatly improved by coexpression of xylXA, encoding 2-keto-3-deoxy-d-xylonate dehydratase and α-ketoglutaric semialdehyde dehydrogenase, respectively. The endogenous periplasmic glucose dehydrogenase (Gcd) of P. putida S12 was found to play a key role in efficient oxidative d-xylose utilization. Gcd activity not only contributes to d-xylose oxidation but also prevents the intracellular accumulation of toxic catabolic intermediates which delays or even eliminates growth on d-xylose.The requirement for renewable alternatives to replace oil-based chemicals and fuels necessitates development of novel technologies. Lignocellulose provides a promising alternative feedstock. However, since the pentose sugar fraction may account for up to 25% of lignocellulosic biomass (12), it is essential that this fraction is utilized efficiently to obtain cost-effective biochemical production. In a previous study, the solvent-tolerant bacterium Pseudomonas putida S12, known for its use as a platform host for the production of aromatic compounds (15, 16, 19, 22), was engineered to use d-xylose as a sole carbon source. This was achieved by introducing genes encoding the phosphorylative d-xylose metabolic pathway of Escherichia coli, followed by laboratory evolution (14). Prior to evolutionary improvement, extensive oxidation of d-xylose to d-xylonate occurred, resulting in a very low biomass-for-substrate yield as d-xylonate is a metabolic dead-end product in P. putida. The evolution approach resulted in elimination of the activity of periplasmic glucose dehydrogenase (Gcd), the enzyme responsible for d-xylose oxidation, which turned out to be a critical step in optimizing phosphorylative d-xylose utilization in P. putida S12.Instead of prevention of endogenous oxidation of d-xylose, this oxidation may be used to our advantage when it is combined with an oxidative d-xylose metabolic pathway, such as the pathways described for several Pseudomonas species, Caulobacter crescentus, and Haloarcula marismortui (7, 11, 18, 20). In these pathways, d-xylonate is dehydrated to 2-keto-3-deoxy-d-xylonate. This intermediate either can be cleaved into pyruvate and glycolaldehyde (7) or is further dehydrated to α-ketoglutaric semialdehyde (α-KGSA). In the final step of the latter pathway, α-KGSA is oxidized to the tricarboxylic acid (TCA) cycle intermediate α-ketoglutarate (18, 20).In addition to Gcd (PP1444), some of the enzymes required for oxidative d-xylose metabolism are expected to be endogenous in P. putida S12. Transport of d-xylonate into the cytoplasm likely occurs through the gluconate transporter (encoded by gntP [PP3417]). The enzyme catalyzing the final step of the pathway, α-KGSA dehydrogenase, is also likely to be present (presumably PP1256 and/or PP3602) because of the requirement for metabolism of 4-hydroxyproline (1), a compound that is efficiently utilized by P. putida S12. In view of these properties, the most obvious approach for constructing d-xylose-utilizing P. putida S12 is reconstruction of a complete oxidative d-xylose metabolic pathway by introducing the parts of such a pathway that complement the endogenous activities. Recently, the genetic information for one such oxidative d-xylose pathway has become available (18), enabling the approach used in the present study, i.e., expression of the oxidative d-xylose metabolic pathway of C. crescentus in P. putida S12 and investigation of the contribution of endogenous enzyme activities.     

Effect of solvent adaptation on the antibiotic resistance in Pseudomonas putida S12

The effect of the adaptation to toluene on the␣resistance to different antibiotics was investigated in the␣solvent-resistant strain Pseudomonas putida S12. We␣followed the process of the solvent adaptation of P.␣putida S12 by cultivating the strain in the presence␣of␣increasing concentrations of toluene and studied␣the correlation of this gradual adaptation to the resistance towards antibiotics. It was shown that the tolerance to various chemically and structurally unrelated antibiotics, with different targets in the cell, increased during this gradual adaptation. The survival of P. putida S12 in the presence of antibiotics like tetracycline, nigericin, polymyxin B, piperacillin or chloramphenicol increased 30- to and 1000-fold after adaptation to 600 mg/l toluene. However, cells grown in the absence of any solvents lost their adaptation to toluene even when grown in the presence of antibiotics. Results are discussed in terms of the physico-chemical properties of membranes as affected by the observed cis/trans isomerization of unsaturated fatty acids, as well as in terms of the active efflux of molecules from the cytoplasmic membrane. Received: 9 May 1997 / Received revision: 4 July 1997 / Accepted: 4 July 1997     

Testosterone 15beta-hydroxylation by solvent tolerant Pseudomonas putida S12

A steroid 15beta-hydroxylating whole-cell solvent tolerant biocatalyst was constructed by expressing the Bacillus megaterium steroid hydroxylase CYP106A2 in the solvent tolerant Pseudomonas putida S12. Testosterone hydroxylation was improved by a factor 16 by co-expressing Fer, a putative Fe-S protein from Bacillus subtilis. In addition, the specificity for 15beta-hydroxylation was improved by mutating threonine residue 248 of CYP106A2 into valine. These new insights provide the basis for an optimized whole-cell steroid-hydroxylating biocatalyst that can be applied with an organic solvent phase.     

Effect of organic solvents on the yield of solvent-tolerant Pseudomonas putida S12.

Solvent-tolerant microorganisms are useful in biotransformations with whole cells in two-phase solvent-water systems. The results presented here describe the effects that organic solvents have on the growth of these organisms. The maximal growth rate of Pseudomonas putida S12, 0.8 h-1, was not affected by toluene in batch cultures, but in chemostat cultures the solvent decreased the maximal growth rate by nearly 50%. Toluene, ethylbenzene, propylbenzene, xylene, hexane, and cyclohexane reduced the biomass yield, and this effect depended on the concentration of the solvent in the bacterial membrane and not on its chemical structure. The dose response to solvents in terms of yield was linear up to an approximately 200 mM concentration of solvent in the bacterial membrane, both in the wild type and in a mutant lacking an active efflux system for toluene. Above this critical concentration the yield of the wild type remained constant at 0.2 g of protein/g of glucose with increasing concentrations of toluene. The reduction of the yield in the presence of solvents is due to a maintenance higher by a factor of three or four as well as to a decrease of the maximum growth yield by 33%. Therefore, energy-consuming adaptation processes as well as the uncoupling effect of the solvents reduce the yield of the tolerant cells.     

Production of pectolytic enzymes fromErwinia grown on different carbon sources

A quantitative analysis of pectolytic enzymes (polygalacturonase (PG), pectin methyl esterase (PME) and six isoenzymes of pectate lyase (PL)) produced byErwinia bacteria in the presence of diverse carbon sources was made by preparative electrophoresis. Synthesis of each of these enzymes was regulated independently; different induction and repression ratios (about 10- to 1000-fold) were observed for diverse PL isoenzymes, PG and PME. The possibility of using specially constructed media for the production of pectinase complexes with a specific spectra of pectolytic enzymes has been demonstrated.     

Bioproduction of p-hydroxybenzoate from renewable feedstock by solvent-tolerant Pseudomonas putida S12

Pseudomonas putida strain S12palB1 was constructed that produces p-hydroxybenzoate from renewable carbon sources via the central metabolite l-tyrosine. P. putida S12palB1 was based on the platform strain P. putida S12TPL3, which has an optimised carbon flux towards l-tyrosine. Phenylalanine ammonia lyase (Pal) was introduced for the conversion of l-tyrosine into p-coumarate, which is further converted into p-hydroxybenzoate by endogenous enzymes. p-Hydroxybenzoate hydroxylase (PobA) was inactivated to prevent the degradation of p-hydroxybenzoate. These modifications resulted in stable accumulation of p-hydroxybenzoate at a yield of 11% (C-molC-mol(-1)) on glucose or on glycerol in shake flask cultures. In a glycerol-limited fed-batch fermentation, a final p-hydroxybenzoate concentration of 12.9mM (1.8gl(-1)) was obtained, at a yield of 8.5% (C-molC-mol(-1)). A 2-fold increase of the specific p-hydroxybenzoate production rate (q(p)) was observed when l-tyrosine was supplied to a steady-state C-limited chemostat culture of P. putida S12palB1. This implied that l-tyrosine availability was the bottleneck for p-hydroxybenzoate production under these conditions. When p-coumarate was added instead, q(p) increased by a factor 4.7, indicating that Pal activity is the limiting factor when sufficient l-tyrosine is available. Thus, two major leads for further improvement of the p-hydroxybenzoate production by P. putida S12palB1 were identified.     

Engineering Pseudomonas putida S12 for efficient utilization of D-xylose and L-arabinose

The solvent-tolerant bacterium Pseudomonas putida S12 was engineered to utilize xylose as a substrate by expressing xylose isomerase (XylA) and xylulokinase (XylB) from Escherichia coli. The initial yield on xylose was low (9% [g CDW g substrate(-1)], where CDW is cell dry weight), and the growth rate was poor (0.01 h(-1)). The main cause of the low yield was the oxidation of xylose into the dead-end product xylonate by endogenous glucose dehydrogenase (Gcd). Subjecting the XylAB-expressing P. putida S12 to laboratory evolution yielded a strain that efficiently utilized xylose (yield, 52% [g CDW g xylose(-1)]) at a considerably improved growth rate (0.35 h(-1)). The high yield could be attributed in part to Gcd inactivity, whereas the improved growth rate may be connected to alterations in the primary metabolism. Surprisingly, without any further engineering, the evolved D-xylose-utilizing strain metabolized l-arabinose as efficiently as D-xylose. Furthermore, despite the loss of Gcd activity, the ability to utilize glucose was not affected. Thus, a P. putida S12-derived strain was obtained that efficiently utilizes the three main sugars present in lignocellulosic hydrolysate: glucose, xylose, and arabinose. This strain will form the basis for a platform host for the efficient production of biochemicals from renewable feedstock.     

Physiological response of Pseudomonas putida S12 subjected to reduced water activity

Abstract The effect of osmotic stress, given as decreased water activity (a_w), on growth and the accumulation of potassium and the compatible solute betaine by Pseudomonas putida S12 was investigated. Reduced a_w was imposed by addition of sodium chloride, sucrose, glycerol or polyethylene glycol to the growth medium. Accumulation of potassium and betaine was established when sodium chloride and sucrose were used to cause osmotic stress. No accumulation of these solutes was found in the presence of glycerol. Addition of polyethylene glycol to the medium strongly decreased the growth rate in comparison with the other osmolytes tested at the corresponding a_w. Although polyethylene glycol did decrease the a_w, neither potassium nor betaine was accumulated by the cells.     

True cellulase production by Clostridium thermocellum grown on different carbon sources

Summary Clostridium thermocellum produced different levels of true cellulase (Avicelase) depending on the carbon source used for growth. In defined medium with fructose, the cellulase titer was seven times higher than with cells growing on cellobiose and four times higher than cells growing with glucose. During the lag phase on fructose, the differences were even more dramatic, i.e. 60 times higher than in cells growing on cellobiose and 40 times that of cells lagging or growing in glucose. In an attempt to detect factors that might contribute to these differences, we considered intracellular ATP, chemical potential (pH), electrical potential (Y), proton motive force (p), growth rate, and rates of uptake of inorganic phosphate and sugars. We noted a direct correlation between cellulase production and intracellular ATP levels and an inverse relationship of cellulase production with Y and p values. It thus appears that cellulase is best produced by cells high in ATP and low in Dp and its electrical component DY. There was no obvious relationship between the cellulase titer and the other parameters. Although the physiological significance of such correlations is unknown, the data suggest that further investigation is warranted.     

The production of antifungal metabolites by Pseudomonas chlororaphis grown on different nutrient sources

It was found that the antifungal activity of Pseudomonas chlororaphis SPB1217 is due to phenazine-1-carboxylic acid, phenazine-1-carboxamide, and two unidentified exometabolites. The carbon source used for the growth of this bacterial strain and iron ions present in the medium considerably influenced the proportion between the antifungal metabolites. The maximum production of phenazines was observed in the media enriched in amino acids and iron ions. The absence of correlation between the production of phenazines and antifungal activity indicates that phenazines are not the only antifungal metabolites of the strain. Organic acids as nutrient sources provide for more intense production of exometabolites and for a higher level of antifungal activity than do sugars.     

An insertion sequence prepares Pseudomonas putida S12 for severe solvent stress

The novel insertion sequence ISS12 plays a key role in the tolerance of Pseudomonas putida S12 to sudden toluene stress. Under normal culturing conditions the P. putida S12 genome contained seven copies of ISS12. However, a P. putida S12 population growing to high cell density after sudden addition of a separate phase of toluene carried eight copies. The survival frequency of cells in this variant P. putida S12 population was 1000 times higher than in "normal" P. putida S12 populations. Analysis of the nucleotide sequence flanking the extra ISS12 insertion revealed integration into the srpS gene. srpS forms a gene cluster with srpR and both are putative regulators of the solvent resistance pump SrpABC. SrpABC makes a major contribution to solvent tolerance in P. putida S12 and is induced by toluene. The basal level of srp promoter activity in the P. putida S12 variant was seven times higher than in wild-type P. putida S12. Introduction of the intact srpRS gene cluster in the variant resulted in a dramatic decrease of survival frequency after a toluene shock. These findings strongly suggest that interruption of srpS by ISS12 up-regulates expression of the solvent pump, enabling the bacterium to tolerate sudden exposure to lethal concentrations of toxic solvents. We propose that P. putida S12 employs ISS12 as a mutator element to generate diverse mutations to swiftly adapt when confronted with severe adverse conditions.     

Engineering of solvent-tolerant Pseudomonas putida S12 for bioproduction of phenol from glucose

Efficient bioconversion of glucose to phenol via the central metabolite tyrosine was achieved in the solvent-tolerant strain Pseudomonas putida S12. The tpl gene from Pantoea agglomerans, encoding tyrosine phenol lyase, was introduced into P. putida S12 to enable phenol production. Tyrosine availability was a bottleneck for efficient production. The production host was optimized by overexpressing the aroF-1 gene, which codes for the first enzyme in the tyrosine biosynthetic pathway, and by random mutagenesis procedures involving selection with the toxic antimetabolites m-fluoro-dl-phenylalanine and m-fluoro-l-tyrosine. High-throughput screening of analogue-resistant mutants obtained in this way yielded a P. putida S12 derivative capable of producing 1.5 mM phenol in a shake flask culture with a yield of 6.7% (mol/mol). In a fed-batch process, the productivity was limited by accumulation of 5 mM phenol in the medium. This toxicity was overcome by use of octanol as an extractant for phenol in a biphasic medium-octanol system. This approach resulted in accumulation of 58 mM phenol in the octanol phase, and there was a twofold increase in the overall production compared to a single-phase fed batch.     

Three distinct quinoprotein alcohol dehydrogenases are expressed when Pseudomonas putida is grown on different alcohols.

A bacterial strain that can utilize several kinds of alcohols as its sole carbon and energy sources was isolated from soil and tentatively identified as Pseudomonas putida HK5. Three distinct dye-linked alcohol dehydrogenases (ADHs), each of which contained the prosthetic group pyrroloquinoline quinone (PQQ), were formed in the soluble fractions of this strain grown on different alcohols. ADH I was formed most abundantly in the cells grown on ethanol and was similar to the quinoprotein ADH reported for P. putida (H. Görisch and M. Rupp, Antonie Leeuwenhoek 56:35-45, 1989) except for its isoelectric point. The other two ADHs, ADH IIB and ADH IIG, were formed separately in the cells grown on 1-butanol and 1,2-propanediol, respectively. Both of these enzymes contained heme c in addition to PQQ and functioned as quinohemoprotein dehydrogenases. Potassium ferricyanide was an available electron acceptor for ADHs IIB and IIG but not for ADH I. The molecular weights were estimated to be 69,000 for ADH IIB and 72,000 for ADH IIG, and both enzymes were shown to be monomers. Antibodies raised against each of the purified ADHs could distinguish the ADHs from one another. Immunoblot analysis showed that ADH I was detected in cells grown on each alcohol tested, but ethanol was the most effective inducer. ADH IIB was formed in the cells grown on alcohols of medium chain length and also on 1,3-butanediol. Induction of ADH IIG was restricted to 1,2-propanediol or glycerol, of which the former alcohol was more effective. These results from immunoblot analysis correlated well with the substrate specificities of the respective enzymes. Thus, three distinct quinoprotein ADHs were shown to be synthesized by a single bacterium under different growth conditions.     

Evaluation of distant carbon sources in biosurfactant production by a gamma ray-induced Pseudomonas putida mutant

Pseudomonas putida 33 wild strain, subjected to gamma ray mutagenesis and designated as P. putida 300-B mutant was used as microbial rhamnolipid-producer by using distant carbon sources (viz. hydrocarbons, waste frying oils ‘WFOs’, vegetable oil refinery wastes and molasses) in the minimal media under shake flask conditions. The behavior of glucose as co-substrate and growth initiator was examined. The 300-B mutant strain showed its ability to grow on all the substrates tested and produced rhamnolipid surfactants to different extents however; soybean and corn WFOs were observed to be preferred carbon sources followed by kerosene and paraffin oils, respectively. The best cell biomass (3.5 g l⁻¹) and rhamnolipids yield (4.1 g l⁻¹) were obtained with soybean WFO as carbon source and glucose as growth initiator under fed-batch cultivation showing an optimum specific growth rate (μ) of 0.272 h⁻¹, specific product yield (q_p) of 0.318 g g⁻¹ h and volumetric productivity (P_V) of 0.024 g l⁻¹ h. The critical micelle concentration of its culture supernatant was observed to be 91 mg rhamnolipids l⁻¹ and surface tension as 31.2 mN m⁻¹.