Pathways of Assimilative Sulfur Metabolism in Pseudomonas putida

Cysteine and methionine biosynthesis was studied in Pseudomonas putida S-313 and Pseudomonas aeruginosa PAO1. Both these organisms used direct sulfhydrylation of O-succinylhomoserine for the synthesis of methionine but also contained substantial levels of O-acetylserine sulfhydrylase (cysteine synthase) activity. The enzymes of the transsulfuration pathway (cystathionine gamma-synthase and cystathionine beta-lyase) were expressed at low levels in both pseudomonads but were strongly upregulated during growth with cysteine as the sole sulfur source. In P. aeruginosa, the reverse transsulfuration pathway between homocysteine and cysteine, with cystathionine as the intermediate, allows P. aeruginosa to grow rapidly with methionine as the sole sulfur source. P. putida S-313 also grew well with methionine as the sulfur source, but no cystathionine gamma-lyase, the key enzyme of the reverse transsulfuration pathway, was found in this species. In the absence of the reverse transsulfuration pathway, P. putida desulfurized methionine by the conversion of methionine to methanethiol, catalyzed by methionine gamma-lyase, which was upregulated under these conditions. A transposon mutant of P. putida that was defective in the alkanesulfonatase locus (ssuD) was unable to grow with either methanesulfonate or methionine as the sulfur source. We therefore propose that in P. putida methionine is converted to methanethiol and then oxidized to methanesulfonate. The sulfonate is then desulfonated by alkanesulfonatase to release sulfite for reassimilation into cysteine.     

p-Hydroxyphenylacetic Acid Metabolism in Pseudomonas putida F6

Pseudomonas putida F6 was found to metabolize p-hydroxyphenylacetic acid through 3,4-dihydroxyphenylacetic acid, 3,4-dihydroxymandelic acid, and 3,4-dihydroxybenzaldehyde. Cell extracts of P. putida F6 catalyze the NAD(P)H-independent hydroxylation of p-hydroxyphenylacetic acid to 3,4-dihydroxyphenylacetic acid which is further oxidized to 3,4-dihydroxymandelic acid. Oxidation and decarboxylation of the latter yields 3,4-dihydroxybenzaldehyde. A red-brown color accompanies all of the above enzyme activities and is probably due to the polymerization of quinone-like compounds. 3,4-Dihydroxybenzaldehyde is further metabolized through extradiol ring cleavage.     

Metabolism of and inhibition by chlorobenzoates in Pseudomonas putida P111.

Pseudomonas putida P111 was isolated by enrichment culture on 2,5-dichlorobenzoate and was also able to grow on 2-chloro-, 3-chloro-, 4-chloro-, 2,3-dichloro-, 2,4-dichloro-, and 2,3,5-trichlorobenzoates. However, 3,5-dichlorobenzoate completely inhibited growth of P111 on all ortho-substituted benzoates that were tested. When 3,5-dichlorobenzoate was added as a cosubstrate with either 3- or 4-chlorobenzoate, cell yields and chloride release were greater than those observed from growth on either monochlorobenzoate alone. Moreover, resting cells of P111 grown on 4-chlorobenzoate released chloride from 3,5-dichlorobenzoate and produced no identifiable intermediate. In contrast, resting cells grown on 2,5-dichlorobenzoate metabolized 3,5-dichlorobenzoate without release of chloride and accumulated a degradation product, which was identified as 1-carboxy-1,2-dihydroxy-3,5-dichlorocyclohexadiene on the basis of gas chromatography-mass spectrometry confirmation of its two acid-hydrolyzed products, 3,5- and 2,4-dichlorophenol. Since 3,5-dichlorocatechol was rapidly metabolized by cells grown on 2,5-dichlorobenzoate, it is apparent that 1-carboxy-1,2-dihydroxy-3,5-dichlorocyclohexadiene is not further metabolized by these cells. Moreover, induction of a functional dihyrodiol dehydrogenase would not be required for growth of P111 on other ortho-chlorobenzoates since the corresponding chlorodihydrodiols produced from a 1,2-dioxygenase attack would spontaneously decompose to the corresponding catechols. In contrast, growth on 3-chloro-, 4-chloro-, or 3,5-dichlorobenzoate requires a functional dihydrodiol dehydrogenase, yet only the two monochlorobenzoates appear to induce for it.     

Phenol and Benzoate Metabolism by Pseudomonas putida: Regulation of Tangential Pathways

Catechol occurs as an intermediate in the metabolism of both benzoate and phenol by strains of Pseudomonas putida. During growth at the expense of benzoate, catechol is cleaved ortho (1,2-oxygenase) and metabolized via the beta-ketoadipate pathway; during growth at the expense of phenol or cresols, the catechol or substituted catechols formed are metabolized by a separate pathway following meta (2,3-oxygenase) cleavage of the aromatic ring of catechol. It is possible to explain the mutually exclusive occurrence of the meta and ortho pathway enzymes in phenol- and benzoate-grown cells of P. putida on the basis of differences in the mode of regulation of these two pathways. By use of both nonmetabolizable inducers and blocked mutants, gratuitous synthesis of some of the meta pathway enzymes was obtained. All four enzymes of the meta pathway are induced by the primary substrate, cresol or phenol, or its analogue. Three enzymes of the ortho pathway that catalyze the conversion of catechol to beta-ketoadipate enol-lactone are induced by cis,cis-muconate, produced from catechol by 1,2-oxygenase-mediated cleavage. Observations on the differences in specificity of induction and function of the two pathways suggest that they are not really either tangential or redundant. The meta pathway serves as a general mechanism for catabolism of various alkyl derivatives of catechol derived from substituted phenolic compounds. The ortho pathway is more specific and serves primarily in the catabolism of precursors of catechol and catechol itself.     

Metabolism of and inhibition by chlorobenzoates in Pseudomonas putida P111.

Pseudomonas putida P111 was isolated by enrichment culture on 2,5-dichlorobenzoate and was also able to grow on 2-chloro-, 3-chloro-, 4-chloro-, 2,3-dichloro-, 2,4-dichloro-, and 2,3,5-trichlorobenzoates. However, 3,5-dichlorobenzoate completely inhibited growth of P111 on all ortho-substituted benzoates that were tested. When 3,5-dichlorobenzoate was added as a cosubstrate with either 3- or 4-chlorobenzoate, cell yields and chloride release were greater than those observed from growth on either monochlorobenzoate alone. Moreover, resting cells of P111 grown on 4-chlorobenzoate released chloride from 3,5-dichlorobenzoate and produced no identifiable intermediate. In contrast, resting cells grown on 2,5-dichlorobenzoate metabolized 3,5-dichlorobenzoate without release of chloride and accumulated a degradation product, which was identified as 1-carboxy-1,2-dihydroxy-3,5-dichlorocyclohexadiene on the basis of gas chromatography-mass spectrometry confirmation of its two acid-hydrolyzed products, 3,5- and 2,4-dichlorophenol. Since 3,5-dichlorocatechol was rapidly metabolized by cells grown on 2,5-dichlorobenzoate, it is apparent that 1-carboxy-1,2-dihydroxy-3,5-dichlorocyclohexadiene is not further metabolized by these cells. Moreover, induction of a functional dihyrodiol dehydrogenase would not be required for growth of P111 on other ortho-chlorobenzoates since the corresponding chlorodihydrodiols produced from a 1,2-dioxygenase attack would spontaneously decompose to the corresponding catechols. In contrast, growth on 3-chloro-, 4-chloro-, or 3,5-dichlorobenzoate requires a functional dihydrodiol dehydrogenase, yet only the two monochlorobenzoates appear to induce for it.     

Metabolism of resorcinylic compounds by bacteria: orcinol pathway in Pseudomonas putida.

Enrichment cultures yielded two strains of Pseudomonas putida capable of growth with orcinol (3,5-dihydroxytoluene) as the sole source of carbon. Experiments with cell suspensions and cell extracts indicate that orcinol is metabolized by hydroxylation of the benzene ring followed successively by ring cleavage and hydrolyses to give 2 mol of acetate and 1 mol of pyruvate per mol of orcinol as shown: orcinol leads to 2,3,5-trihydroxytoluene leads to 2,4,6-trioxoheptanoate leads to acetate + acetylpyruvate leads to acetate + pyruvate. Evidence for this pathway is based on: (i) high respiratory activities of orcinol-grown cells towards 2,3,5-trihydroxytoluene; (ii) transient accumulation of a quinone, probably 2-hydroxy-6-methyl-1,4-benzoquinone, during grouth with orcinol; (iii) formation of pyruvate and acetate from orcinol, 2,3,5-trihydroxytoluene, and acetylpyruvate catalyzed by extracts of orcinol, but not by succinate-grown cells; (iv) characterization of the product of oxidation of 3-methylcatechol (an analogue of 2,3,5-trihydroxytoluene) showing that oxygenative cleavage occurs between carbons bearing methyl and hydroxyl substituents; (v) transient appearance of a compound having spectral properties similar to those of acetylpyruvate during 2,3,5-trihydroxytoluene oxidation by extracts of orcinol-grown cells. Orcinol hydroxylase exhibits catalytic activity when resorcinol or m-cresol is substituted for orcinol; hydroxyquinol and 3-methylcatechol are substrates for the ring cleavage enzyme 2,3,5-trihydroxytoluene-1,2-oxygenase. The enzymes of this pathway are induced by growth with orcinol but not with glucose or succinate.     

Metabolism of amino acid amides in Pseudomonas putida ATCC 12633

The metabolism of the natural amino acid l-valine, the unnatural amino acids d-valine, and d-, l-phenyglycine (d-, l-PG), and the unnatural amino acid amides d-, l-phenylglycine amide (d-, l-PG-NH₂) and l-valine amide (l-Val-NH₂) was studied in Pseudomonas putida ATCC 12633. The organism possessed constitutive l-amidase activities towards l-PG-NH₂ and l-Val-NH₂, both following the same pattern of expression, suggesting the involvement of similarly regulated enzymes, or a common enzyme. Quite surprisingly, growth in mineral media with l-PG-NH₂ resulted in variable, long lag phases of growth and strongly reduced l-amidase activities. Conversion of d-PG-NH₂ into d-PG and l-PG also occurred and could be attributed to the presence of an inducible d-amidase and the racemization of the amino acid amide in combination with l-amidase activity, respectively. The further degradation of l-PG and d-PG involved constitutive l-PG aminotransferase and inducible d-PG dehydrogenase activities, respectively, both with a high degree of enantioselectivity. Amino acid racemase activity for d- and l-PG was not detected. Correspondence to: L. Dijkhuizen     

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.     

Transport of succinate by Pseudomonas putida

Induced succinate uptake and transport (defined as transport of a compound followed by its metabolism and transport in the absence of subsequent metabolism) by Pseudomonas putida are active processes resulting in intracellular succinate concentrations 10-fold that of the initial extracellular concentration. Uptake was studied with the wild-type strain P. putida P2 and transport with a mutant deficient in succinate dehydrogenase activity. Addition of succinate, fumarate, or malate to the growth medium induces both processes above a basal level. Induction is dependent on protein synthesis and subject to catabolite repression. When extracts of induced and noninduced wild-type cells were assayed for succinate dehydrogenase, fumarase, and malate dehydrogenase only malate dehydrogenase increased in specific activity. Transport is inhibited by iodoacetamide, KCN, NaN₃, and 2,4-dinitrophenol and shows pH and temperature optima of 6.2 and 30 °C. Kinetic parameters are: basal uptake (cells grown on glutamate) K_m 11.6 μm, v 0.32 nmoles per min per mg dry cell mass; induced uptake (cells grown on succinate plus NH₄Cl) K_m 12.5 μm, v 5.78 nmoles per min per mg dry cell mass; induced transport (cells grown on nutrient broth plus succinate) K_m 10 μm, V 0.98 nmoles per min per mg dry cell mass. It was not possible to determine the kinetic parameters of basal transport. Malate and fumarate were the only compounds exhibiting competitive inhibition of uptake and transport suggesting common transport system for all three compounds. The K_i values for competitive inhibition and the K_m for succinate indicate the order of affinity for both uptake and transport are succinate > malate > fumarate. Data from kinetic parameters of uptake and transport and studies on succinate metabolism provide evidence consistent with concurrent increases in transport and metabolism to account for induced succinate uptake by P. putida.     

Formation of Filaments by Pseudomonas putida

When Pseudomonas putida 40 was grown on a variety of liquid media in which oxygen became a limiting factor during growth, the latter stages of growth involved the elongation of cells without septation, which can result in the complete filamentation of the culture (up to several hundred micrometers long). The filaments appeared to consist of a chain of protoplasts within a common sacculus. Later these filaments were capable of a rapid fragmentation by septation to give a population of ordinary rods with a corresponding increase in the number of viable particles but no appreciable change in total bacterial mass. Filamentation did not occur if slow growth rates were maintained by restriction of oxygen availability from the beginning of growth. In complex media filaments were not formed during growth on 1% peptone alone, but the addition of 0.1 M phosphate or 6.6 × 10⁻⁴ M EDTA induced extensive filamentation that was reversed by the addition of 6.6 × 10⁻⁴ M Mg²⁺. In minimal media a much higher Mg²⁺ concentration than that required for active growth or present in the complex media was usually required for filamentation. A very narrow range of Mg²⁺ concentration promoted filamentation, and this optimum differed markedly depending on the carbon source used. Other medium variations which influenced the level of filamentation are reported. We found that most strains of P. putida (including the neotype strain) and P. fluorescens gave filaments under the conditions developed with strain 40, whereas several strains of P. aeruginosa failed to give filaments on the same media.     

Biodegradation of Ethylene Glycol by a Salt-Requiring Bacterium

A gram-negative nonmotile rod which was capable of using 1,2-(14)C-ethylene glycol as a sole carbon source for growth was isolated from a brine pond, Great Salt Lake, Utah. The bacterium (ATCC 27042) required at least 0.85% NaCl for growth and, although the chloride ion was replaceable by sulfate ion, the sodium ion was not replaceable by potassium ion. The maximal concentration of salt tolerated for growth was approximately 12%. The bacterium was oxidase-negative when N,N-dimethyl-p-phenylenediamine was used and weakly positive when N,N,N',N'-tetramethyl-p-phenylenediamine was used. It grows on many sugars but does not ferment them, it does not have an exogenous vitamin requirement, and it possesses a guanine plus cytosine ratio of 64.3%. Incorporation of ethylene glycol carbon into cell and respired CO(2) was quantitated by use of radioactive ethylene glycol and a force-aerated fermentor. Glucose suppressed ethylene glycol metabolism. Cells grown on ethylene and propylene glycol respired ethylene glycol in a Warburg respirometer more rapidly than cells grown on glucose. Spectrophotometric evidence was obtained for oxidation of glycolate to glyoxylate by a dialyzed cell extract.     

Biotransformation of limonene by Pseudomonas putida

From a study of three fungal and 15 bacterial strains, it was observed that Pseudomonas putida MTCC 1072 oxidized limonene with the highest efficiency of. Fermentation of limonene by P. putida MTCC 1072 was conducted for 120 h at 30 degrees C at a fixed pH of 5.0. Major bioconversion products were isolated and characterized by Fourier transform infrared (FTIR) and nuclear magnetic resonance (NMR) spectroscopy, and by elemental analysis. The bioconversion products were identified as perillyl alcohol and p-menth-1-ene-6,8-diol, and under optimum conditions the yields were 36% and 44%, respectively (a rate kinetic model indicated corresponding limiting yields of 44% and 56%). No further degradation of the products was observed using this bacteria.     

Degradation of dibenzothiophene by Pseudomonas putida

The microbial degradation of dibenzothiophene (DBT) and other organosulphur compounds such as thiophene-2-carboxylate (T2C) is of interest for the potential desulphurization of coal. The feasibility of degradation of DBT and T2C by Pseudomonas putida and other bacteria was analysed. Pseudomonas putida oxidized sulphur from DBT in the presence of yeast extract, but it did not when DBT was the sole source of carbon.     

alpha-Pinene metabolism by Pseudomonas putida.

By using metabolically altered mutants and acrylate, novel putative intermediates of alpha-pinene metabolism by Pseudomonas putida PIN11 were detected. They were characterized as 3-isopropylbut-3-enoic acid and (zeta)-2-methyl-5-isopropylhexa-2,5-dienoic acid.     

Oxidation of Ethylene Glycol by a Salt-Requiring Bacterium

Bacterium T-52, cultured on ethylene glycol, readily oxidized glycolate and glyoxylate and exhibited elevated activities of ethylene glycol dehydrogenase and glycolate oxidase. Labeled glyoxylate was identified in reaction mixtures containing [¹⁴C]-ethylene glycol, but no glycolate was detected. The most likely pathway of ethylene glycol catabolism by bacterium T-52 is sequential oxidation to glycolate and glyoxylate.     

Peptide utilization by Pseudomonas putida and Pseudomonas maltophilia.

Pseudomonas putida assimilates peptides and hydrolyses them with intracellular peptidases. Amino acid auxotrophs (his, trp, thr or met) grew on a variety of di- and tripeptides up to twice as slowly as with free amino acids. Pseudomonas putida has separate uptake systems for both dipeptides and oligopeptides (three or more residues). Although the dipeptide system transported a variety of structurally diverse dipeptides it did not transport peptides having either unprotonatable N-terminal amino groups, blocked C-terminal carboxyl groups, D-residues, three or more residues, N-methylated peptide bonds, or beta-amino acids. Oligopeptide uptake lacked amino acid side-chain specificity, required a free N-terminal L-residue and had an upper size limit. Glycylglycyl-D,L-p-fluorophenylalanine inhibited growth of P. putida. Uptake of glycylglycyl[I-14C]alanine was rapid and inhibited by 2,4-dinitrophenol. Both dipeptide and oligopeptide uptake were constitutive. Dipeptides competed with oligopeptides for oligopeptide uptake, but oligopeptides did not compete in the dipeptide system. Final bacterial yields were 5 to 10 times greater when P. putida his was grown on histidyl di- or tripeptides rather than on free histidine because the histidyl residue was protected from catabolism by L-histidine ammonia-lyase. Methionine peptides could satisfy the methionine requirements of P. maltophilia. Generation times on glycylmethionine and glycylmethionylglycine were equal to those obtained with free methionine. Methionylglycylmethionylmethionine gave a generation time twice that of free methionine. Growth of P. maltophilia was inhibited by glycylglycyl-D,L-p-fluorophenylalanine.     

Metabolism of Pipecolic Acid in a Pseudomonas Species IV. Electron Transport Particle of Pseudomonas putida

Baginsky, Marietta L. (University of California, San Francisco Medical Center, San Francisco), and Victor W. Rodwell. Metabolism of pipecolic acid in a Pseudomonas species. IV. Electron transport particle of Pseudomonas putida. J. Bacteriol. 92:424-432. 1966.-Enzymes of Pseudomonas putida P2 catalyzing oxidation of pipecolate to Delta(1)-piperideine-6-carboxylate are located in a subcellular fraction sedimenting at 105,000 x g. Since this fraction resembles the mammalian electron transport particle in both chemical composition and enzymatic activities, it was termed Pseudomonas P2 electron transport particle (P2-ETP). P2-ETP contains flavin adenine dinucleotide, flavin mononucleotide, iron, copper, and both b- and c-type cytochromes. The reduced type b cytochrome has absorption maxima at 558 to 559, 530, and 427 mmu. Its oxidized pyridine hemochromogen has an absorption maximum at 406 mmu, with a shoulder at 564 mmu. On dithionite reduction, absorption bands with maxima at 556, 522, and 418 mmu are obtained. The reduced type c cytochrome has absorption maxima at 552, 520, and 422 mmu; its reduced pyridine hemochromogen has maxima at 551, 516 to 519, and 418 mmu. No type a cytochrome was detected. P2-ETP catalyzes oxidation of pipecolate and of reduced nicotinamide adenine dinucleotide (NADH(2)) by oxygen. It can also oxidize these compounds, as well as succinate and reduced nicotinamide adenine dinucleotide phosphate, with 2,6-dichlorophenol-indophenol as electron acceptor. Mammalian cytochrome c can be used as an alternate artificial electron acceptor for the oxidation of pipecolate and succinate, but not for oxidation of NADH(2).