Integrated bioprocess for the oxidation of limonene to perillic acid with Pseudomonas putida DSM 12264

An efficient integrated bioprocess for the oxidation of limonene to perillic acid with Pseudomonas putida DSM 12264 was developed. Perillic acid is a promising candidate for natural preservation and pharmaceutical application. At elevated concentrations the monoterpenoic acid inhibits growth and biotransformation activity of P. putida DSM 12264. The maximum growth rate showed a linear decrease from μ = 1.43 h^?1 in the absence of perillic acid to complete inhibition at 165 ± 7 mM perillic acid. The maximum specific activity of limonene-transforming resting cells revealed an exponential decrease from almost 8 U/g cdw without perillic acid to <0.5 U/g cdw at >25 mM perillic acid. A method for in situ product recovery (ISPR) based on anion exchange resin was established to overcome product inhibition. A column containing a fluidized bed of Amberlite IRA 410 Cl was coupled to the bioreactor and enabled product removal by continuously recirculating the unfiltered broth through the ISPR unit. This led to a cumulative perillic acid concentration of 187 mM (31 g/L) after 7 days, which represents the highest product concentration achieved in a microbial monoterpene oxyfunctionalization so far. The ISPR approach reduced the further downstream processing steps needed which yielded a 93% pure product with a loss of 2%.     

Limonene bioconversion to high concentrations of a single and stable product, perillic acid, by a solvent-resistant Pseudomonas putida strain

The white-rot basidiomycete Phanerochaete chrysosporium BKM-F-1767 was tested for its capacity to degrade dehydroabietic acid (DHA). In anaerobic treatment, this molecule is the most recalcitrant member of the resin acid group, which is known to cause operational problems to anaerobic reactors treating pulp and paper industry wastewaters. In this study the effect of DHA on different parameters, such as growth, ligninolytic enzyme activity, extracellular protein production as well as both glycerol and ammonium consumption by the fungus, was determined. Although the above parameters were affected by the addition of DHA, the results show that the fungus could still produce significant titres of ligninolytic enzymes. The fungus removed 47% of the DHA initially present in the static culture, after 10 days of incubation. Anaerobic toxicity assays showed that the treatment of DHA with P. chrysosporium reduced the methanogenesis and acetogenesis inhibition caused by DHA and allowed improved methane production by the anaerobic bacteria. Received: 10 June 1997 / Received revision: 6 January 1998 / Accepted: 24 January 1998     

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.     

Toluene bioconversion to p-hydroxybenzoate by fed-batch cultures of recombinant Pseudomonas putida.

A microbial oxidation process for the production of p-hydroxybenzoate (HBA) from toluene is reported. The oxidation reaction was studied in fed-batch fermentations using a recombinant Pseudomonas putida grown on glutamate as the sole carbon and energy source with salicylate and IPTG induction of tmoABCDE, and pchCF and phbz pathway genes, respectively. An average volumetric HBA productivity of 13.4 mg HBA x L(-1) x h(-1) was obtained under rapid growth conditions (glutamate excess), giving an HBA titer of 132 mg x L(-1) after 9.8 h of fermentation. This corresponded to an average specific HBA productivity of 7.2 microg HBA (mg total protein)(-1) x h(-1). In contrast, maximum HBA titers of 35 mg HBA x L(-1) were achieved in 27 h in comparative studies employing glutumate limited fed-batch cultures. A specific productivity of 4.1 microg HBA (mg total protein)(-1) x h(-1) and volumetric productivity of 1.3 mg HBA x L(-1) x h(-1) were calculated for the growth-rate restricted cultures. The differences in HBA production between the two cultures could be correlated to the levels of specific toluene-4-monooxygenase (T4MO) polypeptides. T4MO catalyzes the rate-limiting step in the pathway. Using experimental data, the half-life value of TmoA was calculated to be approximately 28 h. Assuming linear, monomolecular decay of TmoA, a specific degradation constant of 0.025 x h(-1) was calculated, which placed the stability of recombinant TmoA in the range of relatively stable proteins, even in the absence of co-expression of tmoF, the terminal oxidoreductase subunit of T4MO.     

Phenol biodegradation by Pseudomonas putida DSM 548 in a batch reactor

Phenol biodegradation in a batch reactor using a pure culture of Pseudomonas putida DSM 548 was studied. The purpose of the experiments was to determine the kinetics of biodegradation by measuring biomass growth rates and phenol concentration as a function of time in a batch reactor. The Haldane equation μ=μ(m)S/((K(s)+S+S(2))/K(i)) adequately describes cell growth with kinetic constants μ(m)=0.436h(-1), K(s)=6.19mgl(-1), K(i)=54.1mgl(-1). These values are in the range of those published in literature for pure or mixed cultures degrading phenol.     

Acetopyruvate hydrolase production by Pseudomonas putida O1--optimization of batch and fed-batch fermentations

The main objective of this work was the optimization of the production of the beta-ketolase, acetopyruvate hydrolase, from Pseudomonas putida O1. Orcinol was used as an inducer for enzyme production. The growth medium was optimized in two steps. In the first step, screening for optimal glucose concentration was performed. In the second step, a central composite design was used to optimize carbon and nitrogen sources in the medium. After this optimization procedure, a medium was obtained which produced seven times more biomass than the initial medium. Acetopyruvate hydrolase enzyme production was optimized by determining the optimal time of feed and amount of orcinol, using statistical methods. In a subsequent step, the maximal orcinol-degradation rate was determined. The results obtained were used to find an optimal feeding profile for enzyme production. By using the optimized fed-batch process, acetopyruvate hydrolase activity was enhanced from 10 units l(-1)to 400 units l(-1), in comparison with previously reported fermentation experiments. Productivity could even be increased by a factor of 75, to a value of 20 units l(-1 )h(-1).     

Expression of recombinant Pseudomonas stutzeri di-heme cytochrome c4 by high-cell-density fed-batch cultivation of Pseudomonas putida

The gene of the di-heme protein cytochrome c(4) from Pseudomonas stutzeri was expressed in Pseudomonas putida. High-yield expression of the protein was achieved by high-cell-density fed-batch cultivation using an exponential glucose feeding strategy. The recombinant cytochrome c(4) protein was purified to apparent homogeneity and analyzed by electronic absorption spectroscopy, nanoflow electrospray ionization time-of-flight mass spectrometry, and electrochemistry. Cyclic voltammograms and UV-vis electronic absorption spectra were indistinguishable from the equivalent data of native P. stutzeri cytochrome c(4). Furthermore, the calculated and experimentally determined molecular masses of recombinant cytochrome c(4) were identical. Biochemical characterization of both wild-type and mutant derivatives of the protein will be greatly enhanced and facilitated by the described high-yield fermentation and rapid isolation procedure.     

pH-stat fed-batch process to enhance the production of cis, cis-muconate from benzoate by Pseudomonas putida KT2440-JD1

Pseudomonas putida KT2440-JD1 is able to cometabolize benzoate to cis, cis-muconate in the presence of glucose as growth substrate. P. putida KT2440-JD1 was unable to grow in the presence of concentrations above 50 mM benzoate or 600 mM cis, cis-muconate. The inhibitory effects of both compounds were cumulative. The maximum specific uptake rate of benzoate was higher than the specific production rate of cis, cis-muconate during growth on glucose in the presence of benzoate, indicating that a benzoate derivative accumulated in the cells, which is likely to be catechol. Catechol was shown to reduce the expression level of the ben operon, which encodes the conversion of benzoate to cis, cis-muconate. To prevent overdoses of benzoate, a pH-stat fed-batch process for the production of cis, cis-muconate from benzoate was developed, in which the addition of benzoate was coupled to the acidification of the medium. The maximum specific production rate during the pH-stat fed-batch process was 0.6 g (4.3 mmol) g dry cell weight(-1) h(-1), whereas 18.5 g L(-1) cis, cis-muconate accumulated in the culture medium with a molar product yield of close to 100%. Proteome analysis revealed that the outer membrane protein H1 was upregulated during the pH-stat fed-batch process, whereas the expression of 10 other proteins was reduced. The identified proteins are involved in energy household, transport, translation of RNA, and motility.     

Enantioselective oxidations catalyzed by diketocamphane monooxygenase from Pseudomonas putida with macromolecular NAD in a membrane reactor

Summary Several sulfides and bicyclo[3.2.0]hept-2-en-6-one were enantioselectively oxidized to the corresponding sulfoxides and oxa lactones by a crude preparation of the two diketocamphane monooxygenases from Pseudomonas putida. The reactions were carried out in a membrane reactor with the use of poly(ethylene glycol)-N⁶-(2-aminoethyl)-NAD and coenzyme regeneration by the formate/formate dehydrogenase system.     

Response of Pseudomonas putida KT2440 to increased NADH and ATP demand

Adenosine phosphate and NAD cofactors play a vital role in the operation of cell metabolism, and their levels and ratios are carefully regulated in tight ranges. Perturbations of the consumption of these metabolites might have a great impact on cell metabolism and physiology. Here, we investigated the impact of increased ATP hydrolysis and NADH oxidation rates on the metabolism of Pseudomonas putida KT2440 by titration of 2,4-dinitrophenol (DNP) and overproduction of a water-forming NADH oxidase, respectively. Both perturbations resulted in a reduction of the biomass yield and, as a consequence of the uncoupling of catabolic and anabolic activities, in an amplification of the net NADH regeneration rate. However, a stimulation of the specific carbon uptake rate was observed only when P. putida was challenged with very high 2,4-dinitrophenol concentrations and was comparatively unaffected by recombinant NADH oxidase activity. This behavior contrasts with the comparably sensitive performance described, for example, for Escherichia coli or Saccharomyces cerevisiae. The apparent robustness of P. putida metabolism indicates that it possesses a certain buffering capacity and a high flexibility to adapt to and counteract different stresses without showing a distinct phenotype. These findings are important, e.g., for the development of whole-cell redox biocatalytic processes that impose equivalent burdens on the cell metabolism: stoichiometric consumption of (reduced) redox cofactors and increased energy expenditures, due to the toxicity of the biocatalytic compounds.     

Biotransformation of styrenes by a Pseudomonas putida

Summary A strain of Pseudomonas putida was isolated from soil in the presence of -methylstyrene, as the sole carbon and energy source. The analysis of the oxidation products from culture broth allowed the identification of 2-phenyl-2-propen-1-ol and 1,2-dihydroxy-3-isopropenyl-3-cyclohexene suggesting the existence of different initial steps in the metabolism of -methylstyrene. The same strain also oxidized styrene and produced by initial oxidation of the aromatic nucleus a compound identified as 1,2-dihydroxy-3-ethenyl-3-cyclohexene.     

Bioconversion of waste office paper to gluconic acid in a turbine blade reactor by the filamentous fungus Aspergillus niger

Gluconic acid production was investigated using an enzymatic hydrolysate of waste office automation paper in a culture of Aspergillus niger. In repeated batch cultures using flasks, saccharified solution medium (SM) did not show any inhibitory effects on gluconic acid production compared to glucose medium (GM). The average gluconic acid yields were 92% (SM) and 80% (GM). In repeated batch cultures using SM in a turbine blade reactor (TBR), the gluconic acid yields were 60% (SM) and 67% (GM) with 80-100 g/l of gluconic acid. When pure oxygen was supplied the production rate increased to four times higher than when supplying air. Remarkable differences in the morphology of A. niger and dry cell weight between SM and GM were observed. The difference in morphology may have caused a reduction of oxygen transfer, resulting in a decrease in gluconic acid production rate in SM.     

Enzymatic synthesis of L-pipecolic acid by Delta1-piperideine-2-carboxylate reductase from Pseudomonas putida

L-Pipecolic acid is a chiral pharmaceutical intermediate. An enzymatic system for the synthesis of L-pipecolic acid from L-lysine by commercial L-lysine alpha-oxidase from Trichoderma viride and an extract of recombinant Escherichia coli cells coexpressing Delta1-piperideine-2-carboxylate reductase from Pseudomonas putida and glucose dehydrogenase from Bacillus subtilis is described. A laboratory-scale process provided 27 g/l of L-pipecolic acid in 99.7% e.e.     

Cyclodextrin-enhanced degradation of toluene and p-toluic acid by Pseudomonas putida.

Degradation of an immiscible aromatic solvent, toluene, and a water-soluble aromatic compound, p-toluic acid, by a Pseudomonas putida strain in the presence of beta-cyclodextrin (beta-CD) was investigated. The ability of CDs to interact with hydrophobic organics and form inclusion compounds was exploited in this study to remove or alleviate the toxicities of substrates and consequently to enable or enhance degradation. Liquid toluene was found to be highly toxic to P. putida. However, this phase toxicity was removed when crystalline beta-CD-complexed toluene was provided as the substrate. The latter was fully degraded at a concentration of up to 10 g/liter. Degradation of toluene vapors was enhanced in the presence of beta-CD as a result of reduced molecular toxicity and facilitated absorption of the gaseous substrate. Similarly, beta-CD alleviated the inhibitory effect of p-toluic acid on P. putida. This protective effect of CD was remarkably more prominent when the microbial culture was shock loaded with an otherwise toxic dose of p-toluic acid (1.8 g/liter).